US4748033A - Tea concentrate having freeze thaw stability and enhanced cold water solubility - Google Patents
Tea concentrate having freeze thaw stability and enhanced cold water solubility Download PDFInfo
- Publication number
- US4748033A US4748033A US07/065,086 US6508687A US4748033A US 4748033 A US4748033 A US 4748033A US 6508687 A US6508687 A US 6508687A US 4748033 A US4748033 A US 4748033A
- Authority
- US
- United States
- Prior art keywords
- tea
- concentrate
- tea concentrate
- solids
- weight
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000012141 concentrate Substances 0.000 title claims abstract description 120
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 43
- 239000007787 solid Substances 0.000 claims abstract description 56
- 239000000203 mixture Substances 0.000 claims abstract description 36
- 239000000230 xanthan gum Substances 0.000 claims abstract description 30
- 229920001285 xanthan gum Polymers 0.000 claims abstract description 30
- 235000010493 xanthan gum Nutrition 0.000 claims abstract description 30
- 229940082509 xanthan gum Drugs 0.000 claims abstract description 30
- 239000002904 solvent Substances 0.000 claims abstract description 24
- 229920005862 polyol Polymers 0.000 claims abstract description 8
- 150000003077 polyols Chemical class 0.000 claims abstract description 8
- 235000000346 sugar Nutrition 0.000 claims abstract description 8
- 150000008163 sugars Chemical class 0.000 claims abstract description 7
- 229920002678 cellulose Polymers 0.000 claims abstract description 5
- 239000001913 cellulose Substances 0.000 claims abstract description 5
- 229920002907 Guar gum Polymers 0.000 claims abstract description 4
- 229920000161 Locust bean gum Polymers 0.000 claims abstract description 4
- 239000000665 guar gum Substances 0.000 claims abstract description 4
- 235000010417 guar gum Nutrition 0.000 claims abstract description 4
- 229960002154 guar gum Drugs 0.000 claims abstract description 4
- 235000010420 locust bean gum Nutrition 0.000 claims abstract description 4
- 239000000711 locust bean gum Substances 0.000 claims abstract description 4
- 235000008504 concentrate Nutrition 0.000 claims description 115
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 33
- 229920002774 Maltodextrin Polymers 0.000 claims description 16
- 235000014620 theaflavin Nutrition 0.000 claims description 16
- 229920002134 Carboxymethyl cellulose Polymers 0.000 claims description 15
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 14
- 239000001768 carboxy methyl cellulose Substances 0.000 claims description 14
- 235000010948 carboxy methyl cellulose Nutrition 0.000 claims description 14
- 235000019534 high fructose corn syrup Nutrition 0.000 claims description 13
- 235000008118 thearubigins Nutrition 0.000 claims description 13
- 239000008112 carboxymethyl-cellulose Substances 0.000 claims description 11
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 7
- 239000002253 acid Substances 0.000 claims description 6
- IPMYMEWFZKHGAX-UHFFFAOYSA-N Isotheaflavin Natural products OC1CC2=C(O)C=C(O)C=C2OC1C(C1=C2)=CC(O)=C(O)C1=C(O)C(=O)C=C2C1C(O)CC2=C(O)C=C(O)C=C2O1 IPMYMEWFZKHGAX-UHFFFAOYSA-N 0.000 claims description 5
- UXRMWRBWCAGDQB-UHFFFAOYSA-N Theaflavin Natural products C1=CC(C2C(CC3=C(O)C=C(O)C=C3O2)O)=C(O)C(=O)C2=C1C(C1OC3=CC(O)=CC(O)=C3CC1O)=CC(O)=C2O UXRMWRBWCAGDQB-UHFFFAOYSA-N 0.000 claims description 5
- 240000008042 Zea mays Species 0.000 claims description 5
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 claims description 5
- 235000002017 Zea mays subsp mays Nutrition 0.000 claims description 5
- 235000005822 corn Nutrition 0.000 claims description 5
- IPMYMEWFZKHGAX-ZKSIBHASSA-N theaflavin Chemical compound C1=C2C([C@H]3OC4=CC(O)=CC(O)=C4C[C@H]3O)=CC(O)=C(O)C2=C(O)C(=O)C=C1[C@@H]1[C@H](O)CC2=C(O)C=C(O)C=C2O1 IPMYMEWFZKHGAX-ZKSIBHASSA-N 0.000 claims description 5
- 229940026509 theaflavin Drugs 0.000 claims description 5
- 108010011485 Aspartame Proteins 0.000 claims description 4
- 229930091371 Fructose Natural products 0.000 claims description 4
- RFSUNEUAIZKAJO-ARQDHWQXSA-N Fructose Chemical compound OC[C@H]1O[C@](O)(CO)[C@@H](O)[C@@H]1O RFSUNEUAIZKAJO-ARQDHWQXSA-N 0.000 claims description 4
- 239000005715 Fructose Substances 0.000 claims description 4
- 239000000605 aspartame Substances 0.000 claims description 4
- 235000010357 aspartame Nutrition 0.000 claims description 4
- IAOZJIPTCAWIRG-QWRGUYRKSA-N aspartame Chemical group OC(=O)C[C@H](N)C(=O)N[C@H](C(=O)OC)CC1=CC=CC=C1 IAOZJIPTCAWIRG-QWRGUYRKSA-N 0.000 claims description 4
- 229960003438 aspartame Drugs 0.000 claims description 4
- 235000013615 non-nutritive sweetener Nutrition 0.000 claims description 4
- BJEPYKJPYRNKOW-REOHCLBHSA-N (S)-malic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O BJEPYKJPYRNKOW-REOHCLBHSA-N 0.000 claims description 3
- OWEGMIWEEQEYGQ-UHFFFAOYSA-N 100676-05-9 Natural products OC1C(O)C(O)C(CO)OC1OCC1C(O)C(O)C(O)C(OC2C(OC(O)C(O)C2O)CO)O1 OWEGMIWEEQEYGQ-UHFFFAOYSA-N 0.000 claims description 3
- GUBGYTABKSRVRQ-PICCSMPSSA-N Maltose Natural products O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@@H]1O[C@@H]1[C@@H](CO)OC(O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-PICCSMPSSA-N 0.000 claims description 3
- BJEPYKJPYRNKOW-UHFFFAOYSA-N alpha-hydroxysuccinic acid Natural products OC(=O)C(O)CC(O)=O BJEPYKJPYRNKOW-UHFFFAOYSA-N 0.000 claims description 3
- GUBGYTABKSRVRQ-QUYVBRFLSA-N beta-maltose Chemical compound OC[C@H]1O[C@H](O[C@H]2[C@H](O)[C@@H](O)[C@H](O)O[C@@H]2CO)[C@H](O)[C@@H](O)[C@@H]1O GUBGYTABKSRVRQ-QUYVBRFLSA-N 0.000 claims description 3
- 239000001630 malic acid Substances 0.000 claims description 3
- 235000011090 malic acid Nutrition 0.000 claims description 3
- 235000020357 syrup Nutrition 0.000 claims description 3
- 239000006188 syrup Substances 0.000 claims description 3
- 235000005979 Citrus limon Nutrition 0.000 claims description 2
- 244000131522 Citrus pyriformis Species 0.000 claims description 2
- 229920000858 Cyclodextrin Polymers 0.000 claims description 2
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 2
- 229920001100 Polydextrose Polymers 0.000 claims description 2
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 claims description 2
- 229940097362 cyclodextrins Drugs 0.000 claims description 2
- 239000008103 glucose Substances 0.000 claims description 2
- 235000013856 polydextrose Nutrition 0.000 claims description 2
- 229920000223 polyglycerol Polymers 0.000 claims description 2
- 150000005846 sugar alcohols Chemical class 0.000 claims description 2
- 241001122767 Theaceae Species 0.000 claims 28
- 235000013616 tea Nutrition 0.000 abstract description 250
- 244000269722 Thea sinensis Species 0.000 abstract description 203
- 239000000796 flavoring agent Substances 0.000 abstract description 14
- 230000015572 biosynthetic process Effects 0.000 abstract description 13
- 235000019634 flavors Nutrition 0.000 abstract description 12
- 235000019606 astringent taste Nutrition 0.000 abstract description 8
- 235000020341 brewed tea Nutrition 0.000 abstract description 8
- 239000003755 preservative agent Substances 0.000 abstract description 8
- 238000010257 thawing Methods 0.000 abstract description 5
- 125000004122 cyclic group Chemical group 0.000 abstract description 4
- 238000007710 freezing Methods 0.000 abstract description 4
- 230000008014 freezing Effects 0.000 abstract description 4
- 244000000010 microbial pathogen Species 0.000 abstract description 4
- 239000000284 extract Substances 0.000 description 39
- 238000000034 method Methods 0.000 description 19
- 150000008442 polyphenolic compounds Chemical class 0.000 description 12
- 239000000047 product Substances 0.000 description 12
- 239000005913 Maltodextrin Substances 0.000 description 11
- 229940035034 maltodextrin Drugs 0.000 description 11
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 9
- 238000000605 extraction Methods 0.000 description 9
- 238000004128 high performance liquid chromatography Methods 0.000 description 9
- 235000013824 polyphenols Nutrition 0.000 description 9
- 235000006468 Thea sinensis Nutrition 0.000 description 8
- RYYVLZVUVIJVGH-UHFFFAOYSA-N caffeine Chemical compound CN1C(=O)N(C)C(=O)C2=C1N=CN2C RYYVLZVUVIJVGH-UHFFFAOYSA-N 0.000 description 8
- 230000014759 maintenance of location Effects 0.000 description 8
- 239000000243 solution Substances 0.000 description 8
- 235000020279 black tea Nutrition 0.000 description 7
- 239000006071 cream Substances 0.000 description 7
- 230000035622 drinking Effects 0.000 description 7
- 239000007788 liquid Substances 0.000 description 7
- 150000001720 carbohydrates Chemical class 0.000 description 5
- 235000014633 carbohydrates Nutrition 0.000 description 5
- 239000013078 crystal Substances 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000002244 precipitate Substances 0.000 description 5
- 229920001864 tannin Polymers 0.000 description 5
- 235000018553 tannin Nutrition 0.000 description 5
- 239000001648 tannin Substances 0.000 description 5
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 4
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 description 4
- 108090000790 Enzymes Proteins 0.000 description 4
- 102000004190 Enzymes Human genes 0.000 description 4
- LPHGQDQBBGAPDZ-UHFFFAOYSA-N Isocaffeine Natural products CN1C(=O)N(C)C(=O)C2=C1N(C)C=N2 LPHGQDQBBGAPDZ-UHFFFAOYSA-N 0.000 description 4
- 239000012901 Milli-Q water Substances 0.000 description 4
- 239000000654 additive Substances 0.000 description 4
- 235000013361 beverage Nutrition 0.000 description 4
- 229960001948 caffeine Drugs 0.000 description 4
- VJEONQKOZGKCAK-UHFFFAOYSA-N caffeine Natural products CN1C(=O)N(C)C(=O)C2=C1C=CN2C VJEONQKOZGKCAK-UHFFFAOYSA-N 0.000 description 4
- 230000001351 cycling effect Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 229940088598 enzyme Drugs 0.000 description 4
- 235000003599 food sweetener Nutrition 0.000 description 4
- 239000003765 sweetening agent Substances 0.000 description 4
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 3
- 229920000388 Polyphosphate Polymers 0.000 description 3
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 3
- 102000001848 Salivary Proteins and Peptides Human genes 0.000 description 3
- 108010029987 Salivary Proteins and Peptides Proteins 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 235000009569 green tea Nutrition 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- 239000003456 ion exchange resin Substances 0.000 description 3
- 229920003303 ion-exchange polymer Polymers 0.000 description 3
- 230000000813 microbial effect Effects 0.000 description 3
- 239000001205 polyphosphate Substances 0.000 description 3
- 235000011176 polyphosphates Nutrition 0.000 description 3
- 235000019832 sodium triphosphate Nutrition 0.000 description 3
- 239000001577 tetrasodium phosphonato phosphate Substances 0.000 description 3
- XPCTZQVDEJYUGT-UHFFFAOYSA-N 3-hydroxy-2-methyl-4-pyrone Chemical compound CC=1OC=CC(=O)C=1O XPCTZQVDEJYUGT-UHFFFAOYSA-N 0.000 description 2
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 229920003266 Leaf® Polymers 0.000 description 2
- DLRVVLDZNNYCBX-UHFFFAOYSA-N Polydextrose Polymers OC1C(O)C(O)C(CO)OC1OCC1C(O)C(O)C(O)C(O)O1 DLRVVLDZNNYCBX-UHFFFAOYSA-N 0.000 description 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 2
- 229960000583 acetic acid Drugs 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- 238000013019 agitation Methods 0.000 description 2
- 239000011668 ascorbic acid Substances 0.000 description 2
- 235000010323 ascorbic acid Nutrition 0.000 description 2
- 229960005070 ascorbic acid Drugs 0.000 description 2
- 235000019658 bitter taste Nutrition 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 239000002738 chelating agent Substances 0.000 description 2
- 238000005352 clarification Methods 0.000 description 2
- 239000003086 colorant Substances 0.000 description 2
- 235000005911 diet Nutrition 0.000 description 2
- 230000037213 diet Effects 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 239000012362 glacial acetic acid Substances 0.000 description 2
- 239000008233 hard water Substances 0.000 description 2
- -1 hexaglycerol Chemical compound 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 235000010755 mineral Nutrition 0.000 description 2
- 229920001206 natural gum Polymers 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 238000001223 reverse osmosis Methods 0.000 description 2
- 238000005070 sampling Methods 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- FQENQNTWSFEDLI-UHFFFAOYSA-J sodium diphosphate Chemical compound [Na+].[Na+].[Na+].[Na+].[O-]P([O-])(=O)OP([O-])([O-])=O FQENQNTWSFEDLI-UHFFFAOYSA-J 0.000 description 2
- 235000019982 sodium hexametaphosphate Nutrition 0.000 description 2
- GCLGEJMYGQKIIW-UHFFFAOYSA-H sodium hexametaphosphate Chemical compound [Na]OP1(=O)OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])O1 GCLGEJMYGQKIIW-UHFFFAOYSA-H 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 235000019818 tetrasodium diphosphate Nutrition 0.000 description 2
- YAPQBXQYLJRXSA-UHFFFAOYSA-N theobromine Chemical compound CN1C(=O)NC(=O)C2=C1N=CN2C YAPQBXQYLJRXSA-UHFFFAOYSA-N 0.000 description 2
- UNXRWKVEANCORM-UHFFFAOYSA-I triphosphate(5-) Chemical compound [O-]P([O-])(=O)OP([O-])(=O)OP([O-])([O-])=O UNXRWKVEANCORM-UHFFFAOYSA-I 0.000 description 2
- KNIZBZYMVRWQKN-DMTCNVIQSA-N (3s)-3-amino-4-[[(2r)-1-amino-1-oxopropan-2-yl]amino]-4-oxobutanoic acid Chemical class NC(=O)[C@@H](C)NC(=O)[C@@H](N)CC(O)=O KNIZBZYMVRWQKN-DMTCNVIQSA-N 0.000 description 1
- VMQCQYRHANDJBP-IUYQGCFVSA-N (3s)-3-amino-4-[[(2r)-1-amino-3-hydroxy-1-oxopropan-2-yl]amino]-4-oxobutanoic acid Chemical class OC(=O)C[C@H](N)C(=O)N[C@H](CO)C(N)=O VMQCQYRHANDJBP-IUYQGCFVSA-N 0.000 description 1
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- MIDXCONKKJTLDX-UHFFFAOYSA-N 3,5-dimethylcyclopentane-1,2-dione Chemical compound CC1CC(C)C(=O)C1=O MIDXCONKKJTLDX-UHFFFAOYSA-N 0.000 description 1
- ZAMLGGRVTAXBHI-UHFFFAOYSA-N 3-(4-bromophenyl)-3-[(2-methylpropan-2-yl)oxycarbonylamino]propanoic acid Chemical compound CC(C)(C)OC(=O)NC(CC(O)=O)C1=CC=C(Br)C=C1 ZAMLGGRVTAXBHI-UHFFFAOYSA-N 0.000 description 1
- AGNTUZCMJBTHOG-UHFFFAOYSA-N 3-[3-(2,3-dihydroxypropoxy)-2-hydroxypropoxy]propane-1,2-diol Chemical compound OCC(O)COCC(O)COCC(O)CO AGNTUZCMJBTHOG-UHFFFAOYSA-N 0.000 description 1
- WOKDXPHSIQRTJF-UHFFFAOYSA-N 3-[3-[3-[3-[3-[3-[3-[3-[3-(2,3-dihydroxypropoxy)-2-hydroxypropoxy]-2-hydroxypropoxy]-2-hydroxypropoxy]-2-hydroxypropoxy]-2-hydroxypropoxy]-2-hydroxypropoxy]-2-hydroxypropoxy]-2-hydroxypropoxy]propane-1,2-diol Chemical compound OCC(O)COCC(O)COCC(O)COCC(O)COCC(O)COCC(O)COCC(O)COCC(O)COCC(O)COCC(O)CO WOKDXPHSIQRTJF-UHFFFAOYSA-N 0.000 description 1
- MOMKYJPSVWEWPM-UHFFFAOYSA-N 4-(chloromethyl)-2-(4-methylphenyl)-1,3-thiazole Chemical compound C1=CC(C)=CC=C1C1=NC(CCl)=CS1 MOMKYJPSVWEWPM-UHFFFAOYSA-N 0.000 description 1
- YZQCXOFQZKCETR-UWVGGRQHSA-N Asp-Phe Chemical compound OC(=O)C[C@H](N)C(=O)N[C@H](C(O)=O)CC1=CC=CC=C1 YZQCXOFQZKCETR-UWVGGRQHSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 108010059892 Cellulase Proteins 0.000 description 1
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 description 1
- FBPFZTCFMRRESA-KVTDHHQDSA-N D-Mannitol Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-KVTDHHQDSA-N 0.000 description 1
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 description 1
- FEWJPZIEWOKRBE-JCYAYHJZSA-N Dextrotartaric acid Chemical compound OC(=O)[C@H](O)[C@@H](O)C(O)=O FEWJPZIEWOKRBE-JCYAYHJZSA-N 0.000 description 1
- 229920000896 Ethulose Polymers 0.000 description 1
- 239000001859 Ethyl hydroxyethyl cellulose Substances 0.000 description 1
- 239000000940 FEMA 2235 Substances 0.000 description 1
- 229920000663 Hydroxyethyl cellulose Polymers 0.000 description 1
- 239000004354 Hydroxyethyl cellulose Substances 0.000 description 1
- 229920002153 Hydroxypropyl cellulose Polymers 0.000 description 1
- 235000019501 Lemon oil Nutrition 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- HYMLWHLQFGRFIY-UHFFFAOYSA-N Maltol Natural products CC1OC=CC(=O)C1=O HYMLWHLQFGRFIY-UHFFFAOYSA-N 0.000 description 1
- 229930195725 Mannitol Natural products 0.000 description 1
- 108010059820 Polygalacturonase Proteins 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- KDYFGRWQOYBRFD-UHFFFAOYSA-N Succinic acid Natural products OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 description 1
- FEWJPZIEWOKRBE-UHFFFAOYSA-N Tartaric acid Natural products [H+].[H+].[O-]C(=O)C(O)C(O)C([O-])=O FEWJPZIEWOKRBE-UHFFFAOYSA-N 0.000 description 1
- TVXBFESIOXBWNM-UHFFFAOYSA-N Xylitol Natural products OCCC(O)C(O)C(O)CCO TVXBFESIOXBWNM-UHFFFAOYSA-N 0.000 description 1
- YGCFIWIQZPHFLU-UHFFFAOYSA-N acesulfame Chemical compound CC1=CC(=O)NS(=O)(=O)O1 YGCFIWIQZPHFLU-UHFFFAOYSA-N 0.000 description 1
- 229940081735 acetylcellulose Drugs 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 125000005907 alkyl ester group Chemical group 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 229940024606 amino acid Drugs 0.000 description 1
- 235000001014 amino acid Nutrition 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 150000001558 benzoic acid derivatives Chemical class 0.000 description 1
- KDYFGRWQOYBRFD-NUQCWPJISA-N butanedioic acid Chemical compound O[14C](=O)CC[14C](O)=O KDYFGRWQOYBRFD-NUQCWPJISA-N 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 235000013736 caramel Nutrition 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 235000010418 carrageenan Nutrition 0.000 description 1
- 229920001525 carrageenan Polymers 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 229940106157 cellulase Drugs 0.000 description 1
- 229920002301 cellulose acetate Polymers 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- 235000015165 citric acid Nutrition 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 238000010961 commercial manufacture process Methods 0.000 description 1
- 230000000536 complexating effect Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- HCAJEUSONLESMK-UHFFFAOYSA-N cyclohexylsulfamic acid Chemical class OS(=O)(=O)NC1CCCCC1 HCAJEUSONLESMK-UHFFFAOYSA-N 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 235000019326 ethyl hydroxyethyl cellulose Nutrition 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 108010093305 exopolygalacturonase Proteins 0.000 description 1
- 239000001530 fumaric acid Substances 0.000 description 1
- 235000011087 fumaric acid Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229940059442 hemicellulase Drugs 0.000 description 1
- 108010002430 hemicellulase Proteins 0.000 description 1
- 235000011167 hydrochloric acid Nutrition 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 235000019447 hydroxyethyl cellulose Nutrition 0.000 description 1
- 239000001863 hydroxypropyl cellulose Substances 0.000 description 1
- 235000010977 hydroxypropyl cellulose Nutrition 0.000 description 1
- 229920003088 hydroxypropyl methyl cellulose Polymers 0.000 description 1
- 239000001866 hydroxypropyl methyl cellulose Substances 0.000 description 1
- 235000010979 hydroxypropyl methyl cellulose Nutrition 0.000 description 1
- UFVKGYZPFZQRLF-UHFFFAOYSA-N hydroxypropyl methyl cellulose Chemical compound OC1C(O)C(OC)OC(CO)C1OC1C(O)C(O)C(OC2C(C(O)C(OC3C(C(O)C(O)C(CO)O3)O)C(CO)O2)O)C(CO)O1 UFVKGYZPFZQRLF-UHFFFAOYSA-N 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 229960004903 invert sugar Drugs 0.000 description 1
- 150000002605 large molecules Chemical class 0.000 description 1
- 239000004816 latex Substances 0.000 description 1
- 229920000126 latex Polymers 0.000 description 1
- 239000010501 lemon oil Substances 0.000 description 1
- 239000012263 liquid product Substances 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 229940043353 maltol Drugs 0.000 description 1
- 239000000594 mannitol Substances 0.000 description 1
- 235000010355 mannitol Nutrition 0.000 description 1
- 229960001855 mannitol Drugs 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- HEBKCHPVOIAQTA-UHFFFAOYSA-N meso ribitol Natural products OCC(O)C(O)C(O)CO HEBKCHPVOIAQTA-UHFFFAOYSA-N 0.000 description 1
- 229920000609 methyl cellulose Polymers 0.000 description 1
- 239000001923 methylcellulose Substances 0.000 description 1
- 235000010981 methylcellulose Nutrition 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 235000020333 oolong tea Nutrition 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000036961 partial effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920001467 poly(styrenesulfonates) Polymers 0.000 description 1
- 239000001259 polydextrose Substances 0.000 description 1
- 229940035035 polydextrose Drugs 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 235000007686 potassium Nutrition 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000002335 preservative effect Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 235000018102 proteins Nutrition 0.000 description 1
- 230000005180 public health Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 235000019204 saccharin Nutrition 0.000 description 1
- CVHZOJJKTDOEJC-UHFFFAOYSA-N saccharin Chemical compound C1=CC=C2C(=O)NS(=O)(=O)C2=C1 CVHZOJJKTDOEJC-UHFFFAOYSA-N 0.000 description 1
- 229940081974 saccharin Drugs 0.000 description 1
- 239000000901 saccharin and its Na,K and Ca salt Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- WXMKPNITSTVMEF-UHFFFAOYSA-M sodium benzoate Chemical compound [Na+].[O-]C(=O)C1=CC=CC=C1 WXMKPNITSTVMEF-UHFFFAOYSA-M 0.000 description 1
- 239000004299 sodium benzoate Substances 0.000 description 1
- 235000010234 sodium benzoate Nutrition 0.000 description 1
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 1
- 235000017557 sodium bicarbonate Nutrition 0.000 description 1
- 235000019983 sodium metaphosphate Nutrition 0.000 description 1
- 229940048086 sodium pyrophosphate Drugs 0.000 description 1
- 230000003381 solubilizing effect Effects 0.000 description 1
- 239000000600 sorbitol Substances 0.000 description 1
- 229960002920 sorbitol Drugs 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000010561 standard procedure Methods 0.000 description 1
- 239000012086 standard solution Substances 0.000 description 1
- 239000000375 suspending agent Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 108010038851 tannase Proteins 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 239000011975 tartaric acid Substances 0.000 description 1
- 235000002906 tartaric acid Nutrition 0.000 description 1
- 235000019640 taste Nutrition 0.000 description 1
- 229960004559 theobromine Drugs 0.000 description 1
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 1
- 239000012905 visible particle Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 239000000811 xylitol Substances 0.000 description 1
- 235000010447 xylitol Nutrition 0.000 description 1
- 229960002675 xylitol Drugs 0.000 description 1
- HEBKCHPVOIAQTA-SCDXWVJYSA-N xylitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)CO HEBKCHPVOIAQTA-SCDXWVJYSA-N 0.000 description 1
Images
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
- A23F3/00—Tea; Tea substitutes; Preparations thereof
- A23F3/16—Tea extraction; Tea extracts; Treating tea extract; Making instant tea
- A23F3/163—Liquid or semi-liquid tea extract preparations, e.g. gels or liquid extracts in solid capsules
Definitions
- the present invention relates to tea concentrates having stability against flake formation during cyclic freezing and thawing and enhanced solubility when reconstituted with cold tap water.
- Tea creaming occurs during the production of tea extracts in the commercial manufacture of various types of tea products.
- the cream is a precipitate resulting primarily from the formation of polyphenol-caffeine complexes.
- Some components of this cream have limited solubility in cold water which causes clouding of tea beverages.
- a decreaming step is employed in the manufacture of many tea products to precipitate and remove these complexes.
- decreaming methods include adjustments in operating variables, especially temperature, to cause precipitation of the tea cream complexes, followed by centrifugation, filtration or other equivalent techniques to remove the precipitated complexes.
- frozen tea concentrates can also endure cycles of partial thawing and refreezing due to temperature variations in the distribution system, as well as in store and consumer freezers. Even though the majority of tea cream components which cause clouding in cold water are removed during production of the concentrate, additional precipitate can occur due to freeze concentration of the remaining tea solids because of this freeze/thaw cycling.
- ice crystals form in the tea concentrate. The tea solids are rejected by the ice crystals and are concentrated in the boundary layer between the liquid tea phase and the ice crystals. As the concentration of tea solids in this boundary layer increases, the polyphenols present (e.g.
- thearubigins and theaflavins being to interact with themselves and other materials such as caffeine and protein to form larger, heavier complexes which precipitate out as visible flakes when the concentrate is thawed.
- a tea concentrate containing these insoluble flakes even when added to hot water, yields a cloudy tea beverage which has visible particles.
- tea concentrates Even when distributed frozen, tea concentrates may be subjected to warm or nonrefrigerated temperatures for significant lengths of time before use. Accordingly, the tea concentrate needs to be stable against the growth of most microbial pathogens. Most tea extracts have a pH of about 5.0 or higher. At such pHs, a preservative would have to be added to inhibit microbial growth in case the tea concentrate thawed. Preservatives can impart undesired flavor effects. In the absence of preservatives, the tea concentrate needs to have a pH of about 4.6 or less to be stable against the growth of microbial pathogens when nonfrozen.
- a frozen tea concentrate should provide a tea beverage which has a relatively low to moderate astringency.
- Tea tannis polyphenolic compounds of molecular weight 500 to 3000
- salivary proteins in the mouth to form tannin-protein complexes.
- These complexes can precipitate out and give a puckering mouthfeel referred to as astringency.
- Some astringency is desirable from a tea beverage.
- excessive astringency and bitterness from a tea beverage can provide an unpleasant mouthfeel.
- Tea beverages obtained from a frozen tea concentrate should also have a fresh brewed flavor.
- the principle polyphenols of fresh brewed tea are the theaflavins and the thearubigins.
- Theaflavins are believed to contribute to black tea flavor and color.
- Thearubigins are high molecular weight compounds which also contribute flavor and color.
- theaflavins make significant contributions to the flavor and appearance of a tea beverage, they are almost always present in lower amounts than the thearubigins.
- too high a ratio of thearubigins/theaflavins is indicative of a tea beverage having a flat taste and a dull appearance.
- Preferred tea concentrates have a thearubigin:theaflavin ratio similar to that of fresh brewed tea.
- Typical tea beverages have a viscosity of about 1 centipoise or less at 45° F. (7° C.). A higher viscosity tea beverage would provide a much more preferred thicker mouthfeel.
- U.S. Pat. No. 4,051,267 to Jongeling discloses that carrageenans are particularly suitable for suspending and stabilizing tannins (polyphenols) in a tea extract which is transported in a frozen or chilled condition for use in vending machines.
- ThepH of the tea extracts used appears to be at least 4.9 based on the Examples.
- Jongeling also teaches that good suspension and stabilization can be obtained with xanthan gum.
- Jongeling found that even small amounts (less than 1 g. of xanthan gum per 100 ml. of tea extract) increased the viscosity of the tea extract so that the accuracy of dosing in the dispensing machine was impaired.
- the tea concentrate is prepared from a tea extract having a total solids content of 11 to 12% and a pH of 4.8 to 5.0.
- the tea concentrate is preferably raised to a pH of 5.5 by adding sodium bicarbonate and is protected from microbial growth by the inclusion of sodium benzoate.
- the present invention relates to a tea concentrate which has a pH of about 4.6 or less at 20° C.
- This tea concentrate comprises:
- an edible gum selected from xanthan gum in an amount of from about 5 to about 12% by weight of the tea solids
- natural and modified gums selected from cellulose gums, locust bean gum, guar gum and mixtures thereof in an amount of from about 15 to about 50% by weight of the tea solids
- a preferred optional component of the tea concentrate is a solubilizer selected from the sugars, polyols and mixtures thereof in a weight ratio to the tea solids of from about 0.5 to about 5.
- the edible gum in the tea concentrates of the present invention makes them stable against flake formation during cyclic freezing and thawing. Inclusion of the gum also gives the resulting tea beverage an increased viscosity and therefore an enhanced mouthfeel. Inclusion of the optional solubilizers make the tea concentrate much more cold water soluble.
- the tea concentrates of the present invention are also stableagainst the growth of most microbial pathogens without the use of preservatives due to the relatively low pH. These tea concentrates also provide tea beverages having a fresh brewed tea flavor which are relatively low in astringency and are non-bitter.
- FIG. 1 represents an HPLC chromatograph of the polyphenols present in an ice tea beverage prepared from a tea concentrate made according to the present invention.
- FIG. 2 represents an HPLC chromatograph of the polyphenols present in an ice tea beverage prepared from a commercial bag tea product.
- tea concentrate refers to a product derived from concentrated tea extract which is diluted with water to form a drinkable tea beverage.
- Tea concentrates of the present invention comprise from about 0.4 to about 8% tea solids.
- Preferred tea concentrates of the present invention comprise from about 1 to about 4% by weight tea solids.
- the tea concentrates of the present invention can be in liquid product form but are preferably in frozen product form.
- tea beverage refers to a drinkable beverage prepared from the tea concentrates of the present invention by dilution with water.
- the tea concentrates of the present invention are generally diluted with from about 1 to about 40 parts water to provide the tea beverage.
- Preferred tea concentrates are typically diluted with from about 4 to about 20 parts water to provide the tea beverage.
- tea solids refer to those solids normally present in a tea extract. Polyphenolic compounds are normally the primary component of tea solids. However, tea solids can also include caffeine, theobromine, proteins, amino acids, minerals and carbohydrates.
- flakes refers to insoluble tea solid particles formed at the boundary layer between the liquid tea phase and ice crystals due to freeze concentration of the tea concentrate. These insoluble flakes are extremely difficult to redissolve in cold or hot water without the use of ultrasonic or high shear mixing.
- the term “comprising” means various components can be conjointly employed in the tea concentrates of the present invention. Accordingly, the term “comprising” encompasses the more restrictive terms “consisting essentially of” and “consisting of”.
- the tea concentrates of the present invention are certain edible gums. These edible gums perform at least four functions. The primary function is to prevent the tea polyphenols from forming a concentrated hydrophobic boundary phase between the liquid tea phase and ice crystals during the "freeze" portion of cyclic freezing and thawing of the tea concentrate. This prevents the formation of insoluble flakes that are visible in tea beverages when the tea concentrate is reconstituted with either hot or cold water.
- the gums also perform a second, related function of solubilizing the tea solids of the concentrate when diluted with water to form the tea beverage.
- the other two functions performed by the edible gums are related to mouthfeel effects in the tea beverage.
- the first is enhancing the mouthfeel of the beverage due to an increased actual viscosity.
- tea beverages typically have a viscosity of about 1 centipoise or less at 45° F. (7° C.).
- tea beverages prepared from tea concentrates of the present invention typically have a viscosity of from about 2 to about 10 centipoise at 45° F. (7° C.). This higher viscosity provides a desirable thicker mouthfeel impression.
- the other mouthfeel function is reducing the astringency and perceived bitterness of the tea beverage.
- the gums are believed to aid in complexing the polyphenolic tannins. These tannins, when uncomplexed, are astringent because they bind salivary proteins. However, once the tannins form soluble complexes with the gum, they are much less likely to bind salivary protein. This reduces the astringency of the tea beverage.
- the preferred edible gum for use in the tea concentrates of the present invention is xanthan gum.
- Xanthan gum is preferred because the resulting tea beverage, at drinking strength, has a relatively high pH (about 5.6) which is considered desirable.
- the amount of xanthan gum present in the tea concentrate is from about 5 to about 12% by weight of the tea solids. At levels much below about 5%, xanthan gum alone is not very effective in preventing flake formation during freeze/thaw cycling of the tea concentrate. At levels much above about 12%, the resulting tea beverage has too high a viscosity.
- the amount of xanthan gum included is from about 6 to about 10% by weight of the tea solids.
- modified and natural gums which are useful in the tea concentrates of the present invention are the cellulose gums, locust bean gum, guar gum and mixtures thereof.
- Suitable cellulose gums include methylcellulose, hydroxypropylmethylcellulose, carboxymethylcellulose, hydroxypropylcellulose, hydroxyethylcellulose, ethylhydroxyethylcellulose, and mixtures thereof.
- the preferred cellulose gum is carboxymethylcellulose.
- carboxymethylcellulose provides tea beverages having a pH of about 5.
- these other gums are included in the tea concentrae in an amount of from about 15 to about 50% by weight of the tea solids. At levels much below about 15%, these other gums alone are not very effective in preventing flake formation during freeze/thaw cycling of the tea concentrate. At levels much above about 50%, the resulting tea beverage has too high a viscosity. Preferably, these other gums are included in an amount of from about 20 to about 40% by weight of the tea solids.
- Effective mixtures of xanthan gum with these other natural and modified gums can also be used in tea concentrates of the present invention.
- the term "effective mixture” includes mixtures where xanthan gum is present in an effective amount (from about 5 to about 12% by weight of the tea solids); mixtures where the other modified and natural gums are present in an effective amount (from about 15 to about 50% by weight of the tea solids); mixtures where both the xanthan gum and other gums are present in an effective amount; as well as mixtures of xanthan gum and other gums where neither alone is present in an effective amount but which together provide an effective amount of the edible gum for the purpose of inhibiting formation of insoluble flakes during freeze/thaw cycling of the tea concentrate.
- a mixture of about 4% xanthan gum and about 14% carboxymethylcellulose by weight of the tea solids is an effective mixture within the meaning of the present invention.
- these mixtures comprise xanthan gum in an amount of from about 2 to about 5% by weight of the tea solids, and the other gums in an amount of from about 5 to about 25% by weight of the tea solids.
- a preferred optional component included in the tea concentrates of the present invention is a solubilizer.
- the solubilizer helps to keep the tea solids dissolved in the liquid tea phase to prevent the formation of cream and other precipitates. Inclusion of solubilizers is particularly important if the tea concentrate is to have cold water solubility.
- cold water solubility refers to a tea concentrate which is substantially soluble in water having a temperature of about 20° C. or less. Tea concentrates which contain a solubilizer provide tea beverages having a turbidity of less than about 50 nephelometrics turbidity units (herein NTU).
- tea concentrates of the present invention which do not contain a solubilizer typically provide tea beverages having turbidity values of from about 50 to about 100 NTU. (Turbidity values for the tea beverages resulting from these tea concentrates are measured by the analytical method described hereafter.)
- Solubilizers useful in the tea concentrates of the present invention are selected from sugars, polyols and mixtures thereof.
- Suitable sugars include fructose, glucose, maltose, corn syrups (high fructose corn syrups and high maltose corn syrups), invert sugar, maltodextrins, polydextrose, cyclodextrins and mixtures thereof.
- Preferred sugars for use in the present invention are the high fructose corn syrups and the maltodextrins.
- Suitable polyols for use in tea concentrates of the present include glycerol, propylene glycol, the sugar alcohols such as sorbitol, mannitol, maltol and xylitol, and the polyglycerols such as triglycerol, hexaglycerol, and decaglycerol.
- the preferred polyol for use in the tea concentrates of the present invention is glycerol.
- the solubilizers are included in the tea concentrates of the present invention in a weight ratio to the tea solids of from about 0.5 to about 5.
- the particular amount included will depend upon the solubilizer chosen and the effects desired.
- high fructose corn syrups are preferably included in a weight ratio to tea solids of from about 0.5 to about 2.
- Another preferred sugar solubilizer, maltodextrin is preferably included in a weight ratio to tea solids of from about 0.5 to about 4.
- the preferred polyol solubilizer, glycerol is preferably included in the tea concentrates of the present invention in a weight ratio to tea solids of from about 0.5 to about 2. Care should also be taken to make sure that the solubilizer is not included at a high enough level to cause an off-flavor.
- Certain combinations of edible gums with the solubilizers are especially preferred for use in the tea concentrates of the present invention. These preferred combinations include xanthan gum with high fructose corn syrup; xanthan gum with maltodextrin; xanthan gum with a mixture of high fructose corn syrup and maltodextrin; carboxymethylcellulose with maltodextrin; carboxymethylcellulose with high fructose corn syrup; carboxymethylcellulose with a mixture of maltodextrin and high fructose corn syrup; and a mixture of xanthan gum and carboxymethylcellulose with a mixture of high fructose corn syrup and maltodextrin. These preferred combinations can also contain glycerol.
- the tea concentrates of the present invention have a pH of about 4.6 or less at 20° C., i.e. room temperature. As such, they are essentially stable against the growth of most pathogenic bacteria without the use of preservatives.
- the pH of the tea concentrates of the present invention is from about 2.5 to about 4.6 at 20° C.
- tea extracts used in the preparation of the tea concentrates of the present invention have a pH above 4.6, and typically about 5.0.
- a sutable edible acid can be added in an amount appropriate to lower the pH to about 4.6 or less.
- Suitable edible acids include fumaric acid, citric acid, adipic acid, tartaric acid, succinic acid, malic acid, hydrochloric acid, carbonic acid, ascorbic acid, phosphoric acid, as well as mixtures of these acids (e.g. ascorbic acid and phosphoric acid).
- Malic acid, and especially phosphoric acid are preferred for use in the tea concentrates of the present invention since they provide a tea beverage having a much higher pH when diluted to drinking strength.
- the tea concentrate can also be acidified by contact with an appropriate ion exchange resin.
- suitable ion exchange resins include Dowex HCR-S®, available from Dow Chemical Co.
- a particularly important property of the tea concentrates of the present invention is the fact that they provide tea beverages having a polyphenolic profile similar to that of fresh brewed tea.
- the principle polyphenols in tea are the theaflavins and the thearubigins.
- One adverse effect of the formation of insoluble flakes during freeze/thaw cycles is that the ratio of thearubigins to theaflavins increases with each cycle because the theaflavins are preferentially involved in flake formation.
- the tea concentrates of the present invention maintain a theaflavin content similar to that of fresh brewed tea.
- the tea concentrates of the present invention have a thearubigin to theaflavin ratio of from about 4 to about 8.
- standard fresh brewed teas have a ratio from about 3 to about 10. This ratio is based on the polyphenolic profile of the tea concentrate (or resulting tea beverage) obtained by high pressure liquid chromatography (HPLC) according to a method described hereafter.
- FIG. 1 represents the HPLC chromatograph of a drinking strength iced tea beverage prepared from a tea concentrate made similar to Embodiment 1 of the present invention.
- the retention time (minutes) and area under the curve for each peak of this chromatograph are as follows:
- the peaks at retention times 16.00 through 24.08 minutes are believed to represent the thearubigins and provide a total area of 57,385.
- the peaks at retention times 33.34 through 36.98 minutes are believed to represent the theaflavins and provide a total area of 11,731. The ratio of these total areas is 4.89.
- FIG. 2 represents an HPLC chromatograph of an ice tea beverage freshly prepared from a commercial bag tea product.
- the retention times and area under the curve for each peak are as follows:
- the peaks at retention times 16.14 through 24.09 minutes are believed to represent the thearubigins and provide a total area of 62,243.
- the peaks at retention times 33.24 through 36.79 minutes are believed to represent the theaflavins and provide a total area of 17,870.
- the ratio of these total areas is 3.48.
- Suitable optional ingredients for use in the tea concentrates of the present invention are chelating agents such as ethylenediaminetetraacetic acid (EDTA) or polyphosphates such as sodium metaphosphate, sodium pyrophosphate, tetrasodium pyrophosphate, sodium tripolyphosphate, potassium tripolyphosphate, tetrapotassium polyphosphate, tetrasodiummonopotassium tripolyphosphate, and hexaphos (sodium hexametaphosphate). Inclusion of these agents aids in maintaining tea beverage clarity in hard water. Very low levels of preservatives such as the benzoates and sorbates can also be included to inhibit mold growth. However, tea concentrates of the present invention are typically substantially free of such preservatives.
- EDTA ethylenediaminetetraacetic acid
- polyphosphates such as sodium metaphosphate, sodium pyrophosphate, tetrasodium pyrophosphate, sodium tripolyphosphate, potassium tripo
- the tea concentrates of the present invention can be sweetened or unsweetened.
- the use of the edible gums according to the present invention is particularly useful in preparing diet tea concentrates which contain a sweetening amount of a noncaloric sweetener such as saccharin, cyclamates, acetosulfam, L-aspartyl-L-phenylalanine lower alkyl ester sweeteners (e.g. aspartame), L-aspartyl-D-alanine amides disclosed in U.S. Pat. No. 4,411,925 to Brennan et al., issued Oct. 23, 1983 (herein incorporated by reference), L-aspartyl-D-serine amides disclosed in U.S. Pat. No.
- the tea concentrate of the present invention can also be flavored with various natural or synthetic flavors. Natural and synthetic coloring agents can also be included. Particularly preferred are lemon flavoring (e.g. lemon oil) and caramel coloring. These flavoring and coloring agents are included in the tea concentrates in amounts well known to those skilled in the tea art.
- the tea extracts used in preparing the tea concentrates of the present invention can be obtained from fermented and unfermented teas, e.g., black tea, oolong tea, green tea, or mixtures thereof. Typically, the tea extract is obtained from about 85 to 100% black tea leaves and from 0 to about 15% green tea leaves.
- black tea When black tea is used in preparing the tea extract, it can be enzymatically pretreated according to the method described in European Patent Application No. 135,222 to C. H. Tsai, published May 27, 1985, which is incorporated by reference.
- black tea leaves are wetted with water containing tannase and one or more cell-wall-digesting enzymes, such as cellulase, pectinase, or hemicellulase prior to extraction.
- the enzyme-moistened tea leaves are incubated in a closed system at room temperature for a few hours, neutralized with a suitable foodgrade base and then heated to inactivate the enzymes.
- the resulting enzyme-treated tea leaves provide a higher yield of tea extract which has better solubility in cold water.
- the tea leaves can then be extracted in a conventional manner to provide the tea extract. See Pintauro, Tea and Soluble Tea Products Manufacture (1977), pp. 39-81 (herein incorporated by reference), for various methods of obtaining tea extract from tea leaves.
- the tea leaves are typically slurried with water followed by separation of the leaves from the resulting tea extract.
- This extraction can be performed in a single batch fashion, as a continuous process, as a countercurrent multiple vessel process, or any combination thereof. Continuous countercurrent tea extraction is the most preferred method.
- tea aroma and flavor components can be volatilized from the extract, collected, condensed and added back at a later point in the process.
- the tea desorbate process disclosed in U.S. Pat. No. 4,220,673 to Strobel, issued Sept. 2, 1980 (herein incorporated by reference), can be used to provide the tea extract.
- a tea extraction process which avoids harsh tea flavors and preserves real tea flavor is desirable.
- the tea extract resulting from slurry or countercurrent extraction of tea leaves produces a turbid beverage when diluted with cold water.
- the tea extract is cooled to separate solids which form in a decreaming step. Solids which are precipitated by cooling consist chiefly of tea creams resulting from the formation of complexes of polyphenolic compounds and caffeine. Removal of tea creams is typically achieved by centrifugation, filtration or other suitable means.
- the clarified extract can be further concentrated by suitable methods such as evaporation or reverse osmosis. See Pintauro, supra, pp. 82-141 (herein incorporated by reference), for various representation methods for decreaming, filtering and concentrating tea extracts.
- the edible gums, solubilizers and other optional ingredients can be added at various points in this process.
- some or all of these product additives can be added to the tea extraction water prior to contact with the tea leaves.
- solubilizers to the water used in tea extraction aids in the extraction of theaflavins and other tea components.
- the previously described chelating agents such as EDTA and the polyphosphates can be added to the extraction water to sequester undesired minerals such as calcium and magnesium typically present in hard water and tea leaves.
- the product additives, especially the edible gums and solubilizers can also be added later in this process, such as before or after decreaming and clarification of the tea extract.
- the tea extract after appropriate processing to provide the desired level of tea solids and after the edible gums, solubilizers and optional ingredients have been added, forms the tea concentrate of the present invention.
- This tea concentrate is preferably pasteurized or sterilized prior to packing in containers.
- the tea concentrate product can be distributed as a liquid tea concentrate or else can be chilled to provide a frozen tea concentrate product.
- the polyphenols present in the tea concentrates or tea beverages are analyzed using a modification of the high pressure liquid chromatography procedure described by Hoefler and Coggon, Journal of Chromatography, Vol. 129, (1976), pp. 460-63.
- a DuPont model 8800 liquid chromatographic system (manufactured by DuPont Company, Analytical Instrument Division, Wilmington, DE 19898) with a variable wavelength ultraviolet spectrophotometric detector set at 380 nm is used. Samples are injected onto a chromatographic column using a Dynatech Precision Sampling model LC-241 autosampler (available from Dynotech Precision Sampling, Baton Rouge, LA 70895). A high pressure liquid chromatographic column, Supelco LC-18 3 um ODS, 15 cm ⁇ 4.6 mm (available from Supelco Inc., Bellefonte, PA 16823) is used.
- Chromatographic peaks are recorded using a Spectra-Physics model 4290 recording integrator (available from Spectra-Physics, 3333 N. First St., San Jose, CA 95134). Peak integration is accomplished using a Hewlett-Packard model 1000 computer (available from Hewlett-Packard, 1820 Embarcadero Rd., Palo Alto, CA 94303).
- Mobile phase A consists of 0.24% glacial acetic acid in Milli-Q water (water purified in a Milli-Q Purification Unit, available from Millipore Corp. of Bedford, MA 01730).
- Mobile phase B consists of 50% of 0.24% glacial acetic acid in Milli-Q water and 50% acetone (HPLC grade), available from Burdick & Jackson, 1953 S. Harvey St., Muskegon, MI 49442.
- Samples are eluted in four timed solvent segments: (1) an isocratic segment of 80% mobile phase A and 20% mobile phase B for 2 minutes; (2) a linear gradient from 75% mobile phase A: 25% mobile phase B to 25% mobile phase A: 75% mobile phase B in 30 minutes; (3) an isocratic segment of 10% mobile phase A and 90% mobile phase B for 8 minutes; and (4) an isocratic segment of 80% mobile phase A and 20% mobile phase B for 1 minute.
- Tea solutions containing no carbohydrate additives are first made to drinking strength. An approximate volume of 2 ml is filtered through a 0.45 um cellulose-acetate disposable filter, Millex HA, 25 mm diameter, available from Millipore Corp., Bedford, MA 01730. A 50 ul injection of the filtered solution is made.
- Tea solutions containing carbohydrate additives are sequentially diluted with acetone and water to precipitate the carbohydrates insoluble in mobile phase B.
- the tea concentrate of the present invention is diluted as follows: (1) 1 ml tea concentrate is diluted with 2 ml acetone (source as above); (2) precipitated carbohydrate material is removed with a pasteur pipet; (3) 1 ml of the resultant solution is further diluted with 1.67 ml Milli-Q water; (4) 1 ml of the resulting solution is further diluted with 1 ml Milli-Q water to make a drinking strength solution. Approximately 2 ml of this solution is filtered through a 0.45 um filter, described above, and 50 ul is injected onto the chromatographic column.
- the nephelometric method and nephelometric turbidity unit as described in "Standard Methods for the Examination of Water and Waste Water", 14th ed., published by American Public Health Association, Washington, D.C., is used to determine the cloudiness or turbidity of the tea beverages.
- the turbidity is measured at the refrigerated temperature, i.e. 45° F. (7° C.).
- a blend of 90% black tea leaves (Tender Leaf® blend) and 10% Taiwanese green tea fannings was fed to a Niro® countercurrent extractor (Model A27) at a rate of 0.33 lbs./min. (0.15 kg/min.).
- Distilled water was treated with 0.02% sodium hexametaphosphate and fed into the extractor at a flow rate and temperature of 3.5 lbs./min. (1.6 kg/min.) and 180° F. (82.2° C.), respectively.
- the extract was cooled to a temperature of 124° F. (51.1° C.) at the discharge port of the extractor.
- the extract was passed through a No. 200 (A.S.T.M. Standard) filter screen. This extract had a tea solids concentration of 4.65%.
- the extract was cooled to 85° F. (29.4° C.) and fed to a continuous centrifuge (West Falia Separator Type SA-14-47-076) after a 30 minute hold time at 85° F. (29.4° C.).
- the centrifuge was operated at 7560 rpm. After clarification, the tea solids concentration was 4.15%.
- the extract was diluted with distilled water to a concentration of 3.7% tea solids.
- the frozen concentrate obtained had 3% tea solids, 7% (tea solids basis) of xanthan gum, 107% (tea solids basis) of high fructose corn syrup and 66% (tea solids basis) of maltodextrin.
- One part of the tea concentrate diluted with 15 parts water provided a tea beverage having a turbidity value of 15 NTU and a viscosity of 2.7 centipoise at 45° F. (7° C.).
- the chilled solution is centrifuged with a West Falia Separator (Type SA 14-47-076) at 7560 rpm.
- the clarified extract is concentrated by means of reverse osmosis using D.D.S. HR-98 membranes.
- To this concentrated extract is added various quantities of xanthan gum (XG), carboxymethyl cellulose (CMC), maltodextrin (MD), high fructose corn syrup-55 (HFCS) and glycerol (GLYC), as shown in the following Table:
- the tea concentrates (Embodiments 2 to 7 above) are acidified to pH 4.5 with foodgrade 75% phosphoric acid and then packed into 12 oz. cans after pasteurizing in a Crepaco UHT unit and frozen at 0° F. (-18° C.).
Landscapes
- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Tea And Coffee (AREA)
Abstract
A tea concentrate which is stable against flake formation during cyclic freezing and thawing and which has enhanced solubility in cold water is disclosed. The tea concentrate comprises from about 0.4 to about 8% by weight tea solids, an edible gum selected from xanthan gum, cellulose gums, locust bean gum, guar gum and mixtures thereof in specified amounts, and optionally a solubilizer selected from the sugars, the polyols and mixtures thereof in specified amounts. The tea concentrate has a pH of about 4.6 or less at 20° C. and is therefore stable against the growth of most microbial pathogens without the use of preservatives. Tea beverages prepared from this tea concentrate also have low astringency, fresh brewed tea flavor, and an enhanced mouthfeel.
Description
This is a continuation of application Ser. No. 860,601, filed on May 7, 1986, now abandoned.
The present invention relates to tea concentrates having stability against flake formation during cyclic freezing and thawing and enhanced solubility when reconstituted with cold tap water.
Tea creaming occurs during the production of tea extracts in the commercial manufacture of various types of tea products. The cream is a precipitate resulting primarily from the formation of polyphenol-caffeine complexes. Some components of this cream have limited solubility in cold water which causes clouding of tea beverages.
A decreaming step is employed in the manufacture of many tea products to precipitate and remove these complexes. Several decreaming methods are known in the art. These methods include adjustments in operating variables, especially temperature, to cause precipitation of the tea cream complexes, followed by centrifugation, filtration or other equivalent techniques to remove the precipitated complexes.
During manufacture and sale, frozen tea concentrates can also endure cycles of partial thawing and refreezing due to temperature variations in the distribution system, as well as in store and consumer freezers. Even though the majority of tea cream components which cause clouding in cold water are removed during production of the concentrate, additional precipitate can occur due to freeze concentration of the remaining tea solids because of this freeze/thaw cycling. During the "freeze" portion of the cycle, ice crystals form in the tea concentrate. The tea solids are rejected by the ice crystals and are concentrated in the boundary layer between the liquid tea phase and the ice crystals. As the concentration of tea solids in this boundary layer increases, the polyphenols present (e.g. thearubigins and theaflavins) being to interact with themselves and other materials such as caffeine and protein to form larger, heavier complexes which precipitate out as visible flakes when the concentrate is thawed. A tea concentrate containing these insoluble flakes, even when added to hot water, yields a cloudy tea beverage which has visible particles.
Even when distributed frozen, tea concentrates may be subjected to warm or nonrefrigerated temperatures for significant lengths of time before use. Accordingly, the tea concentrate needs to be stable against the growth of most microbial pathogens. Most tea extracts have a pH of about 5.0 or higher. At such pHs, a preservative would have to be added to inhibit microbial growth in case the tea concentrate thawed. Preservatives can impart undesired flavor effects. In the absence of preservatives, the tea concentrate needs to have a pH of about 4.6 or less to be stable against the growth of microbial pathogens when nonfrozen.
Besides freeze/thaw and microbial stability, a frozen tea concentrate should provide a tea beverage which has a relatively low to moderate astringency. Tea tannis (polyphenolic compounds of molecular weight 500 to 3000) are known to interact with salivary proteins in the mouth to form tannin-protein complexes. These complexes can precipitate out and give a puckering mouthfeel referred to as astringency. Some astringency is desirable from a tea beverage. However, excessive astringency and bitterness from a tea beverage can provide an unpleasant mouthfeel.
Tea beverages obtained from a frozen tea concentrate should also have a fresh brewed flavor. The principle polyphenols of fresh brewed tea are the theaflavins and the thearubigins. Theaflavins are believed to contribute to black tea flavor and color. Thearubigins are high molecular weight compounds which also contribute flavor and color. Although theaflavins make significant contributions to the flavor and appearance of a tea beverage, they are almost always present in lower amounts than the thearubigins. However, too high a ratio of thearubigins/theaflavins is indicative of a tea beverage having a flat taste and a dull appearance. Preferred tea concentrates have a thearubigin:theaflavin ratio similar to that of fresh brewed tea.
An enhanced mouthfeel in a tea beverage obtained from a frozen tea concentrate woudl also be desirable. Typical tea beverages have a viscosity of about 1 centipoise or less at 45° F. (7° C.). A higher viscosity tea beverage would provide a much more preferred thicker mouthfeel.
U.S. Pat. No. 4,051,267 to Jongeling, issued Sept. 27, 1977, discloses that carrageenans are particularly suitable for suspending and stabilizing tannins (polyphenols) in a tea extract which is transported in a frozen or chilled condition for use in vending machines. ThepH of the tea extracts used appears to be at least 4.9 based on the Examples. Jongeling also teaches that good suspension and stabilization can be obtained with xanthan gum. However, Jongeling found that even small amounts (less than 1 g. of xanthan gum per 100 ml. of tea extract) increased the viscosity of the tea extract so that the accuracy of dosing in the dispensing machine was impaired.
U.S. Pat. No. 2,963,368 to Greenbaum, issued Dec. 6, 1960, discloses the use of small proportion of a suspending agent, such as cellulose gum, a solubilizer, such as glycerol, or both, in a tea concentrate to prevent precipitation of remaining caffeine and tannin constituents. The tea concentrate is prepared from a tea extract having a total solids content of 11 to 12% and a pH of 4.8 to 5.0. The tea concentrate is preferably raised to a pH of 5.5 by adding sodium bicarbonate and is protected from microbial growth by the inclusion of sodium benzoate.
The present invention relates to a tea concentrate which has a pH of about 4.6 or less at 20° C. This tea concentrate comprises:
a. from about 0.4 to about 8% by weight tea solids;
b. an edible gum selected from xanthan gum in an amount of from about 5 to about 12% by weight of the tea solids; natural and modified gums selected from cellulose gums, locust bean gum, guar gum and mixtures thereof in an amount of from about 15 to about 50% by weight of the tea solids; and effective mixtures of up to about 12% by weight of the tea solids of xanthan gum and up to about 50% by weight of the tea solids of said natural and modified gums;
c. the balance water.
A preferred optional component of the tea concentrate is a solubilizer selected from the sugars, polyols and mixtures thereof in a weight ratio to the tea solids of from about 0.5 to about 5.
Inclusion of the edible gum in the tea concentrates of the present invention makes them stable against flake formation during cyclic freezing and thawing. Inclusion of the gum also gives the resulting tea beverage an increased viscosity and therefore an enhanced mouthfeel. Inclusion of the optional solubilizers make the tea concentrate much more cold water soluble. The tea concentrates of the present invention are also stableagainst the growth of most microbial pathogens without the use of preservatives due to the relatively low pH. These tea concentrates also provide tea beverages having a fresh brewed tea flavor which are relatively low in astringency and are non-bitter.
FIG. 1 represents an HPLC chromatograph of the polyphenols present in an ice tea beverage prepared from a tea concentrate made according to the present invention.
FIG. 2 represents an HPLC chromatograph of the polyphenols present in an ice tea beverage prepared from a commercial bag tea product.
As used herein, the term "tea concentrate" refers to a product derived from concentrated tea extract which is diluted with water to form a drinkable tea beverage. Tea concentrates of the present invention comprise from about 0.4 to about 8% tea solids. Preferred tea concentrates of the present invention comprise from about 1 to about 4% by weight tea solids. The tea concentrates of the present invention can be in liquid product form but are preferably in frozen product form.
As used herein, the term "tea beverage" refers to a drinkable beverage prepared from the tea concentrates of the present invention by dilution with water. The tea concentrates of the present invention are generally diluted with from about 1 to about 40 parts water to provide the tea beverage. Preferred tea concentrates are typically diluted with from about 4 to about 20 parts water to provide the tea beverage.
As used herein, the term "tea solids" refer to those solids normally present in a tea extract. Polyphenolic compounds are normally the primary component of tea solids. However, tea solids can also include caffeine, theobromine, proteins, amino acids, minerals and carbohydrates.
As used herein, the term "flakes" refers to insoluble tea solid particles formed at the boundary layer between the liquid tea phase and ice crystals due to freeze concentration of the tea concentrate. These insoluble flakes are extremely difficult to redissolve in cold or hot water without the use of ultrasonic or high shear mixing.
As used herein, the term "comprising" means various components can be conjointly employed in the tea concentrates of the present invention. Accordingly, the term "comprising" encompasses the more restrictive terms "consisting essentially of" and "consisting of".
In addition to the tea solids, another key component of the tea concentrates of the present invention are certain edible gums. These edible gums perform at least four functions. The primary function is to prevent the tea polyphenols from forming a concentrated hydrophobic boundary phase between the liquid tea phase and ice crystals during the "freeze" portion of cyclic freezing and thawing of the tea concentrate. This prevents the formation of insoluble flakes that are visible in tea beverages when the tea concentrate is reconstituted with either hot or cold water. The gums also perform a second, related function of solubilizing the tea solids of the concentrate when diluted with water to form the tea beverage.
The other two functions performed by the edible gums are related to mouthfeel effects in the tea beverage. The first is enhancing the mouthfeel of the beverage due to an increased actual viscosity. As previously mentioned, tea beverages typically have a viscosity of about 1 centipoise or less at 45° F. (7° C.). By contrast, tea beverages prepared from tea concentrates of the present invention typically have a viscosity of from about 2 to about 10 centipoise at 45° F. (7° C.). This higher viscosity provides a desirable thicker mouthfeel impression.
The other mouthfeel function is reducing the astringency and perceived bitterness of the tea beverage. The gums are believed to aid in complexing the polyphenolic tannins. These tannins, when uncomplexed, are astringent because they bind salivary proteins. However, once the tannins form soluble complexes with the gum, they are much less likely to bind salivary protein. This reduces the astringency of the tea beverage.
The preferred edible gum for use in the tea concentrates of the present invention is xanthan gum. Xanthan gum is preferred because the resulting tea beverage, at drinking strength, has a relatively high pH (about 5.6) which is considered desirable. When used alone, the amount of xanthan gum present in the tea concentrate is from about 5 to about 12% by weight of the tea solids. At levels much below about 5%, xanthan gum alone is not very effective in preventing flake formation during freeze/thaw cycling of the tea concentrate. At levels much above about 12%, the resulting tea beverage has too high a viscosity. Preferably, the amount of xanthan gum included is from about 6 to about 10% by weight of the tea solids.
Other modified and natural gums which are useful in the tea concentrates of the present invention are the cellulose gums, locust bean gum, guar gum and mixtures thereof. Suitable cellulose gums include methylcellulose, hydroxypropylmethylcellulose, carboxymethylcellulose, hydroxypropylcellulose, hydroxyethylcellulose, ethylhydroxyethylcellulose, and mixtures thereof. The preferred cellulose gum is carboxymethylcellulose. These other gums provide tea concentrates which yield tea beverages having a lower pH at drinking strength than those where xanthan gum is used. For example, carboxymethylcellulose provides tea beverages having a pH of about 5.
When used alone, these other gums (or mixtures thereof) are included in the tea concentrae in an amount of from about 15 to about 50% by weight of the tea solids. At levels much below about 15%, these other gums alone are not very effective in preventing flake formation during freeze/thaw cycling of the tea concentrate. At levels much above about 50%, the resulting tea beverage has too high a viscosity. Preferably, these other gums are included in an amount of from about 20 to about 40% by weight of the tea solids.
Effective mixtures of xanthan gum with these other natural and modified gums can also be used in tea concentrates of the present invention. As used herein, the term "effective mixture" includes mixtures where xanthan gum is present in an effective amount (from about 5 to about 12% by weight of the tea solids); mixtures where the other modified and natural gums are present in an effective amount (from about 15 to about 50% by weight of the tea solids); mixtures where both the xanthan gum and other gums are present in an effective amount; as well as mixtures of xanthan gum and other gums where neither alone is present in an effective amount but which together provide an effective amount of the edible gum for the purpose of inhibiting formation of insoluble flakes during freeze/thaw cycling of the tea concentrate. For example, a mixture of about 4% xanthan gum and about 14% carboxymethylcellulose by weight of the tea solids is an effective mixture within the meaning of the present invention. Typically, these mixtures comprise xanthan gum in an amount of from about 2 to about 5% by weight of the tea solids, and the other gums in an amount of from about 5 to about 25% by weight of the tea solids.
A preferred optional component included in the tea concentrates of the present invention is a solubilizer. The solubilizer helps to keep the tea solids dissolved in the liquid tea phase to prevent the formation of cream and other precipitates. Inclusion of solubilizers is particularly important if the tea concentrate is to have cold water solubility. As used herein, the term "cold water solubility" refers to a tea concentrate which is substantially soluble in water having a temperature of about 20° C. or less. Tea concentrates which contain a solubilizer provide tea beverages having a turbidity of less than about 50 nephelometrics turbidity units (herein NTU). By comparison, tea concentrates of the present invention which do not contain a solubilizer typically provide tea beverages having turbidity values of from about 50 to about 100 NTU. (Turbidity values for the tea beverages resulting from these tea concentrates are measured by the analytical method described hereafter.)
Solubilizers useful in the tea concentrates of the present invention are selected from sugars, polyols and mixtures thereof. Suitable sugars include fructose, glucose, maltose, corn syrups (high fructose corn syrups and high maltose corn syrups), invert sugar, maltodextrins, polydextrose, cyclodextrins and mixtures thereof. Preferred sugars for use in the present invention are the high fructose corn syrups and the maltodextrins. Suitable polyols for use in tea concentrates of the present include glycerol, propylene glycol, the sugar alcohols such as sorbitol, mannitol, maltol and xylitol, and the polyglycerols such as triglycerol, hexaglycerol, and decaglycerol. The preferred polyol for use in the tea concentrates of the present invention is glycerol.
The solubilizers are included in the tea concentrates of the present invention in a weight ratio to the tea solids of from about 0.5 to about 5. The particular amount included will depend upon the solubilizer chosen and the effects desired. For example, high fructose corn syrups are preferably included in a weight ratio to tea solids of from about 0.5 to about 2. Another preferred sugar solubilizer, maltodextrin, is preferably included in a weight ratio to tea solids of from about 0.5 to about 4. The preferred polyol solubilizer, glycerol, is preferably included in the tea concentrates of the present invention in a weight ratio to tea solids of from about 0.5 to about 2. Care should also be taken to make sure that the solubilizer is not included at a high enough level to cause an off-flavor.
Certain combinations of edible gums with the solubilizers are especially preferred for use in the tea concentrates of the present invention. These preferred combinations include xanthan gum with high fructose corn syrup; xanthan gum with maltodextrin; xanthan gum with a mixture of high fructose corn syrup and maltodextrin; carboxymethylcellulose with maltodextrin; carboxymethylcellulose with high fructose corn syrup; carboxymethylcellulose with a mixture of maltodextrin and high fructose corn syrup; and a mixture of xanthan gum and carboxymethylcellulose with a mixture of high fructose corn syrup and maltodextrin. These preferred combinations can also contain glycerol.
The tea concentrates of the present invention have a pH of about 4.6 or less at 20° C., i.e. room temperature. As such, they are essentially stable against the growth of most pathogenic bacteria without the use of preservatives. Typically, the pH of the tea concentrates of the present invention is from about 2.5 to about 4.6 at 20° C. Generally, tea extracts used in the preparation of the tea concentrates of the present invention have a pH above 4.6, and typically about 5.0. To acidify the tea extract for use in the tea concentrates of the present invention a sutable edible acid can be added in an amount appropriate to lower the pH to about 4.6 or less. Suitable edible acids include fumaric acid, citric acid, adipic acid, tartaric acid, succinic acid, malic acid, hydrochloric acid, carbonic acid, ascorbic acid, phosphoric acid, as well as mixtures of these acids (e.g. ascorbic acid and phosphoric acid). Malic acid, and especially phosphoric acid, are preferred for use in the tea concentrates of the present invention since they provide a tea beverage having a much higher pH when diluted to drinking strength. The tea concentrate can also be acidified by contact with an appropriate ion exchange resin. Examples of suitable ion exchange resins include Dowex HCR-S®, available from Dow Chemical Co. of Midland, MI, and Rohm & Haas IRC-50® acid cationic exchange resin available from Rohm & Haas of Philadelphia, PA. Acidification with ion exchange resins is a particularly useful method since the tea concentrate will provide a tea beverage having a much higher pH at drinking strength.
A particularly important property of the tea concentrates of the present invention is the fact that they provide tea beverages having a polyphenolic profile similar to that of fresh brewed tea. As previously mentioned, the principle polyphenols in tea are the theaflavins and the thearubigins. One adverse effect of the formation of insoluble flakes during freeze/thaw cycles is that the ratio of thearubigins to theaflavins increases with each cycle because the theaflavins are preferentially involved in flake formation. Thus, by preventing flake formation, the tea concentrates of the present invention maintain a theaflavin content similar to that of fresh brewed tea. The tea concentrates of the present invention have a thearubigin to theaflavin ratio of from about 4 to about 8. By comparison, standard fresh brewed teas have a ratio from about 3 to about 10. This ratio is based on the polyphenolic profile of the tea concentrate (or resulting tea beverage) obtained by high pressure liquid chromatography (HPLC) according to a method described hereafter.
The similarity in flavor profile between the tea concentrates of the present invention and freshly brewed tea is illustrated by a comparison of the HPLC chromatographs of FIGS. 1 and 2 and especially the thearubigin to theaflavin ratios defined by these chromatographs. FIG. 1 represents the HPLC chromatograph of a drinking strength iced tea beverage prepared from a tea concentrate made similar to Embodiment 1 of the present invention. The retention time (minutes) and area under the curve for each peak of this chromatograph are as follows:
______________________________________ Retention Time Area ______________________________________ 1.07 6507 1.24 1647 1.36 2633 1.65 829 2.04 1650 3.51 164 4.27 1190 6.08 333 6.49 131 10.87 382 12.87 624 13.28 184 13.49 1237 13.97 54 14.52 255 15.24 44 16.00 1569 16.49 4029 17.10 2300 17.90 4110 18.88 1299 19.09 1723 19.48 10485 20.10 6165 20.62 11152 21.18 2623 21.67 368 21.98 258 22.31 549 22.77 1246 23.09 4607 24.08 4902 24.76 414 25.06 569 25.30 330 26.14 315 28.30 346 28.92 697 29.29 190 29.71 249 30.27 274 30.74 115 31.14 120 32.05 573 32.21 618 33.34 5542 34.32 218 34.71 606 35.41 86 36.12 1894 36.57 1625 36.98 1760 38.08 143 38.63 46 40.19 93 42.36 42 ______________________________________
The peaks at retention times 16.00 through 24.08 minutes are believed to represent the thearubigins and provide a total area of 57,385. The peaks at retention times 33.34 through 36.98 minutes are believed to represent the theaflavins and provide a total area of 11,731. The ratio of these total areas is 4.89.
FIG. 2 represents an HPLC chromatograph of an ice tea beverage freshly prepared from a commercial bag tea product. The retention times and area under the curve for each peak are as follows:
______________________________________ Retention Time Area ______________________________________ 1.37 656 1.66 684 2.03 3267 2.45 2912 3.62 199 4.52 2919 6.12 82 6.37 339 6.67 843 7.18 63 8.63 76 9.93 45 10.31 128 11.00 382 11.89 133 13.09 1783 13.35 370 13.58 1345 14.08 81 14.62 214 15.08 272 16.14 1694 16.61 4513 16.93 453 17.19 1631 17.98 2569 18.93 1682 19.18 1967 19.56 11491 20.20 6932 20.70 13261 21.25 1531 21.44 984 21.77 726 22.37 645 22.82 1399 23.12 5143 24.09 5622 24.79 787 25.01 616 25.30 400 26.15 638 27.00 133 28.26 603 28.90 932 29.69 381 30.19 189 30.65 76 32.07 1148 32.83 165 33.24 6821 34.15 274 34.54 773 35.27 441 35.96 3133 36.41 2805 36.79 3623 37.90 208 38.50 49 39.20 46 40.02 50 ______________________________________
The peaks at retention times 16.14 through 24.09 minutes are believed to represent the thearubigins and provide a total area of 62,243. The peaks at retention times 33.24 through 36.79 minutes are believed to represent the theaflavins and provide a total area of 17,870. The ratio of these total areas is 3.48.
Suitable optional ingredients for use in the tea concentrates of the present invention are chelating agents such as ethylenediaminetetraacetic acid (EDTA) or polyphosphates such as sodium metaphosphate, sodium pyrophosphate, tetrasodium pyrophosphate, sodium tripolyphosphate, potassium tripolyphosphate, tetrapotassium polyphosphate, tetrasodiummonopotassium tripolyphosphate, and hexaphos (sodium hexametaphosphate). Inclusion of these agents aids in maintaining tea beverage clarity in hard water. Very low levels of preservatives such as the benzoates and sorbates can also be included to inhibit mold growth. However, tea concentrates of the present invention are typically substantially free of such preservatives.
Generally, the tea concentrates of the present invention can be sweetened or unsweetened. The use of the edible gums according to the present invention is particularly useful in preparing diet tea concentrates which contain a sweetening amount of a noncaloric sweetener such as saccharin, cyclamates, acetosulfam, L-aspartyl-L-phenylalanine lower alkyl ester sweeteners (e.g. aspartame), L-aspartyl-D-alanine amides disclosed in U.S. Pat. No. 4,411,925 to Brennan et al., issued Oct. 23, 1983 (herein incorporated by reference), L-aspartyl-D-serine amides disclosed in U.S. Pat. No. 4,399,163 to Brennan et al., issued Aug. 16, 1983 (herein incorporated by reference), L-aspartyl-L-1-hydroxymethylalkaneamide sweeteners disclosed in U.S. Pat. No. 4,338,346 to Brand, issued Dec. 21, 1982 (herein incorporated by reference), L-aspartyl-1-hydroxyethylalkaneamide sweeteners disclosed in U.S. Pat. No. 4,423,029 to Rizzi, issued Dec. 27, 1983 (herein incorporated by reference), L-aspartyl-D-phenylglycine ester and amide sweeteners disclosed in European Patent Application No. 168,112 to J. M. Janusz, published Jan. 15, 1986 (herein incorporated by reference) and the like. A particularly preferred noncaloric sweetener for use in such diet tea concentrates is aspartame.
The tea concentrate of the present invention can also be flavored with various natural or synthetic flavors. Natural and synthetic coloring agents can also be included. Particularly preferred are lemon flavoring (e.g. lemon oil) and caramel coloring. These flavoring and coloring agents are included in the tea concentrates in amounts well known to those skilled in the tea art.
The tea extracts used in preparing the tea concentrates of the present invention can be obtained from fermented and unfermented teas, e.g., black tea, oolong tea, green tea, or mixtures thereof. Typically, the tea extract is obtained from about 85 to 100% black tea leaves and from 0 to about 15% green tea leaves. When black tea is used in preparing the tea extract, it can be enzymatically pretreated according to the method described in European Patent Application No. 135,222 to C. H. Tsai, published May 27, 1985, which is incorporated by reference. In the Tsai method, black tea leaves are wetted with water containing tannase and one or more cell-wall-digesting enzymes, such as cellulase, pectinase, or hemicellulase prior to extraction. The enzyme-moistened tea leaves are incubated in a closed system at room temperature for a few hours, neutralized with a suitable foodgrade base and then heated to inactivate the enzymes. The resulting enzyme-treated tea leaves provide a higher yield of tea extract which has better solubility in cold water.
The tea leaves, with or without pretreatment with enzymes, can then be extracted in a conventional manner to provide the tea extract. See Pintauro, Tea and Soluble Tea Products Manufacture (1977), pp. 39-81 (herein incorporated by reference), for various methods of obtaining tea extract from tea leaves. The tea leaves are typically slurried with water followed by separation of the leaves from the resulting tea extract. This extraction can be performed in a single batch fashion, as a continuous process, as a countercurrent multiple vessel process, or any combination thereof. Continuous countercurrent tea extraction is the most preferred method. If desired, tea aroma and flavor components can be volatilized from the extract, collected, condensed and added back at a later point in the process. Also, the tea desorbate process disclosed in U.S. Pat. No. 4,220,673 to Strobel, issued Sept. 2, 1980 (herein incorporated by reference), can be used to provide the tea extract. A tea extraction process which avoids harsh tea flavors and preserves real tea flavor is desirable.
The tea extract resulting from slurry or countercurrent extraction of tea leaves produces a turbid beverage when diluted with cold water. Typically, the tea extract is cooled to separate solids which form in a decreaming step. Solids which are precipitated by cooling consist chiefly of tea creams resulting from the formation of complexes of polyphenolic compounds and caffeine. Removal of tea creams is typically achieved by centrifugation, filtration or other suitable means. Depending upon the desired concentration of tea solids in the product, the clarified extract can be further concentrated by suitable methods such as evaporation or reverse osmosis. See Pintauro, supra, pp. 82-141 (herein incorporated by reference), for various representation methods for decreaming, filtering and concentrating tea extracts.
The edible gums, solubilizers and other optional ingredients can be added at various points in this process. For example, some or all of these product additives can be added to the tea extraction water prior to contact with the tea leaves. In particular, the addition of solubilizers to the water used in tea extraction aids in the extraction of theaflavins and other tea components. Also, the previously described chelating agents such as EDTA and the polyphosphates can be added to the extraction water to sequester undesired minerals such as calcium and magnesium typically present in hard water and tea leaves. The product additives, especially the edible gums and solubilizers, can also be added later in this process, such as before or after decreaming and clarification of the tea extract.
The tea extract, after appropriate processing to provide the desired level of tea solids and after the edible gums, solubilizers and optional ingredients have been added, forms the tea concentrate of the present invention. This tea concentrate is preferably pasteurized or sterilized prior to packing in containers. The tea concentrate product can be distributed as a liquid tea concentrate or else can be chilled to provide a frozen tea concentrate product.
The following analytical methods are used in the present application to evaluate the polyphenolic profile and turbidity properties of tea concentrates or tea beverages.
1. Polyphenols
The polyphenols present in the tea concentrates or tea beverages are analyzed using a modification of the high pressure liquid chromatography procedure described by Hoefler and Coggon, Journal of Chromatography, Vol. 129, (1976), pp. 460-63.
A DuPont model 8800 liquid chromatographic system (manufactured by DuPont Company, Analytical Instrument Division, Wilmington, DE 19898) with a variable wavelength ultraviolet spectrophotometric detector set at 380 nm is used. Samples are injected onto a chromatographic column using a Dynatech Precision Sampling model LC-241 autosampler (available from Dynotech Precision Sampling, Baton Rouge, LA 70895). A high pressure liquid chromatographic column, Supelco LC-18 3 um ODS, 15 cm×4.6 mm (available from Supelco Inc., Bellefonte, PA 16823) is used. Chromatographic peaks are recorded using a Spectra-Physics model 4290 recording integrator (available from Spectra-Physics, 3333 N. First St., San Jose, CA 95134). Peak integration is accomplished using a Hewlett-Packard model 1000 computer (available from Hewlett-Packard, 1820 Embarcadero Rd., Palo Alto, CA 94303).
A binary mobile phase system is used. Mobile phase A consists of 0.24% glacial acetic acid in Milli-Q water (water purified in a Milli-Q Purification Unit, available from Millipore Corp. of Bedford, MA 01730). Mobile phase B consists of 50% of 0.24% glacial acetic acid in Milli-Q water and 50% acetone (HPLC grade), available from Burdick & Jackson, 1953 S. Harvey St., Muskegon, MI 49442.
Samples are eluted in four timed solvent segments: (1) an isocratic segment of 80% mobile phase A and 20% mobile phase B for 2 minutes; (2) a linear gradient from 75% mobile phase A: 25% mobile phase B to 25% mobile phase A: 75% mobile phase B in 30 minutes; (3) an isocratic segment of 10% mobile phase A and 90% mobile phase B for 8 minutes; and (4) an isocratic segment of 80% mobile phase A and 20% mobile phase B for 1 minute.
Tea solutions containing no carbohydrate additives are first made to drinking strength. An approximate volume of 2 ml is filtered through a 0.45 um cellulose-acetate disposable filter, Millex HA, 25 mm diameter, available from Millipore Corp., Bedford, MA 01730. A 50 ul injection of the filtered solution is made.
Tea solutions containing carbohydrate additives are sequentially diluted with acetone and water to precipitate the carbohydrates insoluble in mobile phase B. For example, the tea concentrate of the present invention is diluted as follows: (1) 1 ml tea concentrate is diluted with 2 ml acetone (source as above); (2) precipitated carbohydrate material is removed with a pasteur pipet; (3) 1 ml of the resultant solution is further diluted with 1.67 ml Milli-Q water; (4) 1 ml of the resulting solution is further diluted with 1 ml Milli-Q water to make a drinking strength solution. Approximately 2 ml of this solution is filtered through a 0.45 um filter, described above, and 50 ul is injected onto the chromatographic column.
2. Turbidity
The nephelometric method and nephelometric turbidity unit, as described in "Standard Methods for the Examination of Water and Waste Water", 14th ed., published by American Public Health Association, Washington, D.C., is used to determine the cloudiness or turbidity of the tea beverages. A Hach Ratio Turbidimeter, Model 18900-00, available from Hach Chemical Company, Loveland, Col., is employed. It is calibrated prior to each measurement using Latex Standard solutions provided by Hach Chemical Company. For refrigerated beverages, the turbidity is measured at the refrigerated temperature, i.e. 45° F. (7° C.).
The following specific embodiments are used to illustrate the tea concentrates of the present invention:
A blend of 90% black tea leaves (Tender Leaf® blend) and 10% Taiwanese green tea fannings was fed to a Niro® countercurrent extractor (Model A27) at a rate of 0.33 lbs./min. (0.15 kg/min.). Distilled water was treated with 0.02% sodium hexametaphosphate and fed into the extractor at a flow rate and temperature of 3.5 lbs./min. (1.6 kg/min.) and 180° F. (82.2° C.), respectively. The extract was cooled to a temperature of 124° F. (51.1° C.) at the discharge port of the extractor. The extract was passed through a No. 200 (A.S.T.M. Standard) filter screen. This extract had a tea solids concentration of 4.65%.
The extract was cooled to 85° F. (29.4° C.) and fed to a continuous centrifuge (West Falia Separator Type SA-14-47-076) after a 30 minute hold time at 85° F. (29.4° C.). The centrifuge was operated at 7560 rpm. After clarification, the tea solids concentration was 4.15%. The extract was diluted with distilled water to a concentration of 3.7% tea solids.
To 100 lbs. (45.4 kg) of this tea extract was added and mixed 0.27 lbs. (276 grams) Keltrol-T® foodgrade xanthan gum and 2.5 lbs. (1.1 kg) of maltodextrin using a continuous blender (Ladish Co. Triblender, Model No. F2116 MD-S). Then, 4.0 lbs. (1.8 kg) of high fructose corn syrup-55, 0.49 lb. (222 grams) caramel color, and 0.0043 lbs. (1.95 grams) of FD&C Red Dye # 40 were added and mixed in. The pH of the mixture was adjusted to 4.5 using 0.08 lbs. (36.3 grams) of foodgrade 75% phosphoric acid. The tea concentrate was then packed into 4 oz. cans after pasteurizing in a Crepaco UHT unit. The cans were then frozen at -10° F. (-23.3° C.).
The frozen concentrate obtained had 3% tea solids, 7% (tea solids basis) of xanthan gum, 107% (tea solids basis) of high fructose corn syrup and 66% (tea solids basis) of maltodextrin. One part of the tea concentrate diluted with 15 parts water provided a tea beverage having a turbidity value of 15 NTU and a viscosity of 2.7 centipoise at 45° F. (7° C.).
Six hundred and fifty (650) pounds (295.5 kg.) of distilled deaerated water at 70° F. (20° C.) is placed in a stainless steel tank. Thirty-two and one-half (32.5) pounds (14.8 kg.) of black tea leaves (Tender Leaf® blend) are mixed into the water. After constant agitation for 20 minutes, the slurry is allowed to settle for 20 minutes. The mixture is maintained at about 70° F. (21° C.) during this time.
Five hundred (500) pounds (227.3 kg.) of the 70° F. (21° C.) extract are then removed from the leaves by pumping the extract through a No. 200 (A.S.T.M. Standard filter screen. Five hundred (500) pounds (227.3 kg.) of water are added to the residual leaves. This mixture is heated to 180° F. (82° C.) while under constant agitation. Five hundred (500) pounds (227.3 kg.) of tea extract is recovered from the heating tank by deleafing using a West Falia Separator (Type CA 220-010). The deleafed tea extract is mixed with the 70° F. extract, then cooled to 45° F. (7° C.). The chilled solution is centrifuged with a West Falia Separator (Type SA 14-47-076) at 7560 rpm. The clarified extract is concentrated by means of reverse osmosis using D.D.S. HR-98 membranes. To this concentrated extract is added various quantities of xanthan gum (XG), carboxymethyl cellulose (CMC), maltodextrin (MD), high fructose corn syrup-55 (HFCS) and glycerol (GLYC), as shown in the following Table:
______________________________________
Embod- % Tea % % % % %
iment Solids XG* CMC* MD* HFCS* GLYC*
______________________________________
2 0.8 -- 18.8
250 62.5
3 0.8 -- 25 312.5 81.3
4 0.8 6.3 -- -- 100
5 1.07 -- 28 280.3 56.1
6 1.0 -- 38 250 -- 60
7 1.0 0.4 23 250 60 --
______________________________________
The tea concentrates (Embodiments 2 to 7 above) are acidified to pH 4.5 with foodgrade 75% phosphoric acid and then packed into 12 oz. cans after pasteurizing in a Crepaco UHT unit and frozen at 0° F. (-18° C.).
Claims (18)
1. A frozen tea concentrate having a pH of about 4.6 or less at 20° C. and which comprises:
a. from about 0.4 to about 8% by weight decreamed tea solids;
b. an edible gum selected from the group consisting of xanthan gum in an amount of from about 5 to about 12% by weight of said tea solids; natural and modified gums selected from the group consisting of cellulose gums, locust bean gum, guar gum and mixtures thereof in an amount of from about 15 to about 50% by weight of said tea solids; and mixtures of from about 2 to about 5% by weight of said tea solids of said xanthan gum and from about 5 to about 25% by weight of said tea solids of said natural and modified gums;
c. the balance water.
2. The tea concentrate of claim 1 wherein said cellulose gum is carboxymethylcellulose.
3. The tea concentrate of claim 2 wherein said edible gum is carboxymethylcellulose.
4. The tea concentrate of claim 2 wherein said edible gum is xanthan gum.
5. The tea concentrate of claim 1 which further comprises a solubilizer selected from the group consisting of sugars, polyols and mixtures thereof in a weight ratio to said tea solids of from about 0.5 to about 5.
6. The tea concentrate of claim 5 wherein said sugars are selected from the group consisting of glucose, fructose, corn syrups, maltose, maltodextrins, polydextroses and cyclodextrins and wherein said polyols are selected from the group consisting of glycerol, sugar alcohols and polyglycerols.
7. The tea concentrate of claim 6 wherein said solubilizer is selected from the group consisting of high fructose corn syrup, maltodextrins, glycerol and mixtures thereof.
8. The tea concentrate of claim 1 which comprises from about 1 to about 4% by weight of said tea solids.
9. The tea concentrate of claim 1 which further comprises a sweetening amount of a noncaloric sweetener.
10. The tea concentrate of claim 9 wherein said noncaloric sweetener is aspartame.
11. The tea concentrate of claim 1 which is frozen.
12. The tea concentrate of claim 1 which further comprises an edible acid selected from the group consisting of phosphoric acid and malic acid.
13. The tea concentrate of claim 12 wherein said edible acid is phosphoric acid.
14. A frozen tea concentrate having a pH of about 4.6 or less at 20° C. and which comprises:
a. from about 1 to about 4% by weight decreamed tea solids;
b. from about 6 to about 10% by weight of said tea solids of xanthan gum;
c. a solubilizer selected from the group consisting of high fructose corn syrup, maltodextrins, glycerol and mixtures thereof in a weight ratio to said tea solids of from about 0.5 to about 5;
d. the balance water.
15. The tea concentrate of claim 14 which further comprises a sweetening amount of aspartame.
16. The tea concentrate of claim 14 which is frozen.
17. The tea concentrate of claim 14 which further comprises a lemon flavoring.
18. The tea concentrate of claim 1 which has a thearubigin to theaflavin ratio of from about 4 to about 8.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/065,086 US4748033A (en) | 1986-05-07 | 1987-06-18 | Tea concentrate having freeze thaw stability and enhanced cold water solubility |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US86060186A | 1986-05-07 | 1986-05-07 | |
| US07/065,086 US4748033A (en) | 1986-05-07 | 1987-06-18 | Tea concentrate having freeze thaw stability and enhanced cold water solubility |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US86060186A Continuation | 1986-05-07 | 1986-05-07 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US4748033A true US4748033A (en) | 1988-05-31 |
Family
ID=26745192
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US07/065,086 Expired - Lifetime US4748033A (en) | 1986-05-07 | 1987-06-18 | Tea concentrate having freeze thaw stability and enhanced cold water solubility |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US4748033A (en) |
Cited By (59)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4959230A (en) * | 1988-09-27 | 1990-09-25 | Kraft General Foods, Inc. | Composition for extending shelf life of fruits and vegetables |
| US5240732A (en) * | 1990-06-01 | 1993-08-31 | Kabushiki Kaisha Yakult Honsha | Plant extract-containing beverage |
| WO1994014328A1 (en) * | 1992-12-22 | 1994-07-07 | Unilever Plc | Process for manufacturing cold water soluble and chill stable ready to drink tea, and product |
| WO1994014329A1 (en) * | 1992-12-22 | 1994-07-07 | Unilever Plc | Process for manufacturing cold water soluble and chill stable ready to drink tea, and product |
| US5427806A (en) * | 1994-08-08 | 1995-06-27 | The Procter & Gamble Company | Process for making a stable green tea extract and product |
| US5445836A (en) * | 1994-05-12 | 1995-08-29 | Kraft Foods, Inc. | Enzymatic clarification of tea extracts |
| US5523108A (en) * | 1992-04-30 | 1996-06-04 | Wansor; Gerard J. | Unsweetened frozen tea beverage concentrate |
| US5532012A (en) * | 1995-06-02 | 1996-07-02 | Thomas J. Lipton Co., Division Of Conopco, Inc. | Process for preparation of purified tea components using preconcentration by cream separation and solubilization followed by medium pressure chromatography and/or preparative HPLC |
| WO1996026648A1 (en) * | 1995-02-28 | 1996-09-06 | The Procter & Gamble Company | Preparation of noncarbonated beverage products having superior microbial stability |
| USH1628H (en) * | 1994-01-10 | 1997-01-07 | Ekanayake; Athula | Tea extract and process |
| US5612079A (en) * | 1993-11-18 | 1997-03-18 | Nestec S.A. | Preparation of cold-water-soluble instant tea |
| US5641532A (en) * | 1995-12-15 | 1997-06-24 | The Procter & Gamble Company | Beverages having stable flavor/cloud emulsions in the presence of polyphosphate-containing preservative systems by including gellan gum |
| US5681569A (en) * | 1994-06-03 | 1997-10-28 | The Procter & Gamble Company | Beverage compositions containing green tea solids, electrolytes and carbohydrates to provide improved cellular hydration and drinkability |
| WO1998023164A1 (en) * | 1996-11-29 | 1998-06-04 | Unilever Plc | Black leaf tea |
| US5780086A (en) * | 1994-08-08 | 1998-07-14 | The Procter & Gamble Company | Color and shelf stable beverage compositions containing tea extract |
| US5792502A (en) * | 1995-12-15 | 1998-08-11 | The Procter & Gamble Company | Beverages having stable flavor/cloud emulsions in the presence of polyphosphate-containing preservative systems and low levels of xanthan gum |
| EP0891973A1 (en) * | 1997-07-15 | 1999-01-20 | Unilever Plc | Improvements in or relating to producing theaflavin |
| US5879733A (en) * | 1996-02-26 | 1999-03-09 | The Procter & Gamble Company | Green tea extract subjected to cation exchange treatment and nanofiltration to improve clarity and color |
| WO1999021432A1 (en) * | 1997-10-28 | 1999-05-06 | Unilever Plc | Flavouring materials for use in tea containing beverages |
| US5922380A (en) * | 1996-12-12 | 1999-07-13 | Ito En, Ltd. | Tea manufacturing process |
| US6024991A (en) * | 1996-06-19 | 2000-02-15 | Thomas J. Lipton Co., | Tea concentrate prepared by enzymatic extraction and containing xanthan gum which is stable at ambient temperature |
| US6036986A (en) * | 1997-10-28 | 2000-03-14 | Lipton, Division Of Conopco, Inc. | Cinnamic acid for use in tea containing beverages |
| US6036982A (en) * | 1996-06-19 | 2000-03-14 | Thomas J. Lipton Co., Division Of Conopco, Inc. | Enzymatically extracted tea concentrate with xanthan gum which is stable at ambient temperature |
| US6120823A (en) * | 1997-10-28 | 2000-09-19 | Lipton, Divsion Of Conopco, Inc. | Flavoring materials used in foodstuffs |
| US6261619B1 (en) | 1994-02-24 | 2001-07-17 | The Procter & Gamble Co. | Noncarbonated beverage products with improved microbial stability and processes for preparing |
| US6268003B1 (en) | 1994-02-24 | 2001-07-31 | The Procter & Gamble Company | Noncarbonated beverage products with improved microbial stability and processes for preparing |
| US6274187B1 (en) * | 1996-06-19 | 2001-08-14 | Thomas J. Lipton Co., Division Of Conopco, Inc. | Aqueous tea extract concentrate stable at ambient temperature |
| US6294214B1 (en) | 1994-02-24 | 2001-09-25 | The Procter & Gamble Co. | Noncarbonated beverage products with improved microbial stability and processes for preparing |
| US6413570B1 (en) | 1999-02-12 | 2002-07-02 | Lipton, Division Of Conopco, Inc. | Tea concentrate |
| US6468576B1 (en) * | 2000-06-23 | 2002-10-22 | Nestec S.A. | Frozen slush liquid concentrate and method of making same |
| US20020160090A1 (en) * | 2001-04-27 | 2002-10-31 | Pepsico, Inc. | Use of erythritol and D-tagatose in diet or reduced-calorie beverages and food products |
| US20020197371A1 (en) * | 2001-04-27 | 2002-12-26 | Pepsico, Inc. | Use of erythritol and D-tagatose in zero-or low-calorie beverages and food products |
| US20020197379A1 (en) * | 2001-06-08 | 2002-12-26 | Unilever Bestfoods North America, Division Of Conopco, Inc. | Cold water soluble tea concentrate |
| US20030069396A1 (en) * | 1999-11-29 | 2003-04-10 | Masakazu Nishimura | Neutralizing agent for toxin of microorganism belonging to the genus clostridium |
| US20030134017A1 (en) * | 2001-12-19 | 2003-07-17 | The Procter & Gamble Company | Beverage compositions having low levels of preservative with enhanced microbial stability |
| WO2004014142A1 (en) * | 2002-07-31 | 2004-02-19 | Rich Products Corporation | Reduced-calorie freezable beverage |
| WO2004054379A1 (en) * | 2002-12-16 | 2004-07-01 | Council Of Scientific And Industrial Research | A process for preparation of spiced tea concentrate and products thereof |
| US20040265468A1 (en) * | 2003-05-14 | 2004-12-30 | Cheryl Perks | Whippable food product with improved stability |
| US20050025872A1 (en) * | 2003-03-20 | 2005-02-03 | Joseph John F. | Non-dairy whippable food product |
| WO2005053438A1 (en) | 2003-12-03 | 2005-06-16 | Unilever Plc | Tea beverage with improved flavour |
| US20070082106A1 (en) * | 2001-04-27 | 2007-04-12 | Thomas Lee | Use of Erythritol and D-Tagatose In Diet or Reduced-Calorie Beverages and Food Products |
| US20080020115A1 (en) * | 2004-11-30 | 2008-01-24 | Nestec S.A. | Method For Delivering Hot And Cold Beverages On Demand In A Variety Of Flavorings And Nutritional Additives |
| US20080160135A1 (en) * | 2006-12-27 | 2008-07-03 | Conopco, Inc., D/B/A Unilever | Method for Making a Tea Extract and a Tea Extract |
| WO2008082576A1 (en) * | 2006-12-30 | 2008-07-10 | The Coca-Cola Company | Inhibition of the formation of tea opacification or precipitation in tea drinks during storage |
| US20080206429A1 (en) * | 2004-11-30 | 2008-08-28 | Nestec S.A. | Beverage Dispenser With Additive Dispensing |
| US20090092724A1 (en) * | 2007-10-04 | 2009-04-09 | David Mattie | Frozen Slush Drink |
| US20100051501A1 (en) * | 2008-08-29 | 2010-03-04 | International Business Machines Corporation | Ic waper carrier sealed from ambient atmosphere during transportation from one process to the next |
| US20110039009A1 (en) * | 2009-08-11 | 2011-02-17 | Curt Jones | Method and system for flash freezing tea-flavored liquid and making tea-based beverages |
| US20110123700A1 (en) * | 2009-11-25 | 2011-05-26 | Peththawadu Pasan Thijee | Instant liquid tea concentrate |
| US20110143008A1 (en) * | 2007-10-04 | 2011-06-16 | David Mattie | Frozen Slush Drink |
| US20110206808A1 (en) * | 2005-03-03 | 2011-08-25 | Green Rabbit, Llc | Non-dairy, non-soy whippable food product and method of making |
| US8367141B2 (en) * | 2009-12-21 | 2013-02-05 | Kao Corporation | Instant black tea containing green tea extract |
| US20130224365A1 (en) * | 2012-02-28 | 2013-08-29 | Orly AVIDANILOVITCH | Frozen beverage portions |
| WO2013036287A3 (en) * | 2011-09-09 | 2013-10-10 | Kraft Foods Group Brands Llc | Shelf stable, brewed beverage concentrates and methods of making the same |
| WO2015022130A1 (en) * | 2013-08-15 | 2015-02-19 | Unilever N.V. | A process for producing a liquid concentrate tea product |
| WO2015022123A1 (en) * | 2013-08-15 | 2015-02-19 | Unilever N.V. | A process for producing a liquid concentrate tea product |
| US10863754B2 (en) | 2014-07-03 | 2020-12-15 | Kraft Foods Group Brands Llc | Low water coffee and tea beverage concentrates and methods for making the same |
| US20220000139A1 (en) * | 2018-11-27 | 2022-01-06 | Conopco, Inc., D/B/A Unilever | A process of aroma recovery from tea leaf |
| US20220022514A1 (en) * | 2018-12-13 | 2022-01-27 | Societe Des Produits Nestle S.A. | Liquid concentrates formulated for dilution into nutritional products to promote safe swallowing for individuals with dysphagia |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1525272A (en) * | 1921-06-28 | 1925-02-03 | William A Darrah | Extract and method of making same |
| US2476072A (en) * | 1946-06-07 | 1949-07-12 | Donald K Tressler | Method of making a tea extract |
| US2963368A (en) * | 1958-05-28 | 1960-12-06 | Kwik Kafe Coffee Processors Of | Method of producing a tea concentrate |
| US2978328A (en) * | 1958-06-24 | 1961-04-04 | Tea Corp | Process for producing a tea concentrate |
| US3492126A (en) * | 1966-11-09 | 1970-01-27 | Maryland Cup Corp | Soft-frozen whipped aqueous extract concentrate of coffee or tea |
| US3619205A (en) * | 1968-11-20 | 1971-11-09 | Gen Foods Corp | Process of preparing a slush ice beverage concentrate |
| GB1319439A (en) * | 1971-01-22 | 1973-06-06 | Ceylon Inst Of Scient Ind Rese | Preparation of tea extracts suitable for chilled beverages |
| US4051267A (en) * | 1974-09-17 | 1977-09-27 | D.E.J. International Research Company B.V. | Process for stabilizing tea extract and product |
| US4539216A (en) * | 1984-05-25 | 1985-09-03 | The Procter & Gamble Co. | Process for preparing tea products |
-
1987
- 1987-06-18 US US07/065,086 patent/US4748033A/en not_active Expired - Lifetime
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1525272A (en) * | 1921-06-28 | 1925-02-03 | William A Darrah | Extract and method of making same |
| US2476072A (en) * | 1946-06-07 | 1949-07-12 | Donald K Tressler | Method of making a tea extract |
| US2963368A (en) * | 1958-05-28 | 1960-12-06 | Kwik Kafe Coffee Processors Of | Method of producing a tea concentrate |
| US2978328A (en) * | 1958-06-24 | 1961-04-04 | Tea Corp | Process for producing a tea concentrate |
| US3492126A (en) * | 1966-11-09 | 1970-01-27 | Maryland Cup Corp | Soft-frozen whipped aqueous extract concentrate of coffee or tea |
| US3619205A (en) * | 1968-11-20 | 1971-11-09 | Gen Foods Corp | Process of preparing a slush ice beverage concentrate |
| GB1319439A (en) * | 1971-01-22 | 1973-06-06 | Ceylon Inst Of Scient Ind Rese | Preparation of tea extracts suitable for chilled beverages |
| US4051267A (en) * | 1974-09-17 | 1977-09-27 | D.E.J. International Research Company B.V. | Process for stabilizing tea extract and product |
| US4539216A (en) * | 1984-05-25 | 1985-09-03 | The Procter & Gamble Co. | Process for preparing tea products |
Non-Patent Citations (5)
| Title |
|---|
| Andres, "Xanthan Gums Permit High Clarity Solutions", Food Processing, (Nov. 1985), p. 60. |
| Andres, Xanthan Gums Permit High Clarity Solutions , Food Processing, (Nov. 1985), p. 60. * |
| Furia, CRC Handbook of Food Additives, vol. I, (2nd Edition), 1972, pp. 447 448. * |
| Furia, CRC Handbook of Food Additives, vol. I, (2nd Edition), 1972, pp. 447-448. |
| Label, Tetley Iced Tea Concentrate, The Coca Cola Company. * |
Cited By (90)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4959230A (en) * | 1988-09-27 | 1990-09-25 | Kraft General Foods, Inc. | Composition for extending shelf life of fruits and vegetables |
| US5240732A (en) * | 1990-06-01 | 1993-08-31 | Kabushiki Kaisha Yakult Honsha | Plant extract-containing beverage |
| US5523108A (en) * | 1992-04-30 | 1996-06-04 | Wansor; Gerard J. | Unsweetened frozen tea beverage concentrate |
| AU684259B2 (en) * | 1992-12-22 | 1997-12-11 | Unilever Plc | Process for manufacturing cold water soluble and chill stable ready to drink tea, and product |
| WO1994014328A1 (en) * | 1992-12-22 | 1994-07-07 | Unilever Plc | Process for manufacturing cold water soluble and chill stable ready to drink tea, and product |
| WO1994014329A1 (en) * | 1992-12-22 | 1994-07-07 | Unilever Plc | Process for manufacturing cold water soluble and chill stable ready to drink tea, and product |
| US5529796A (en) * | 1992-12-22 | 1996-06-25 | Thomas J. Lipton Co., Division Of Conopco, Inc. | Process for manufacturing cold water soluble and chill stable ready to drink tea and product |
| US5612079A (en) * | 1993-11-18 | 1997-03-18 | Nestec S.A. | Preparation of cold-water-soluble instant tea |
| USH1628H (en) * | 1994-01-10 | 1997-01-07 | Ekanayake; Athula | Tea extract and process |
| US6261619B1 (en) | 1994-02-24 | 2001-07-17 | The Procter & Gamble Co. | Noncarbonated beverage products with improved microbial stability and processes for preparing |
| US6268003B1 (en) | 1994-02-24 | 2001-07-31 | The Procter & Gamble Company | Noncarbonated beverage products with improved microbial stability and processes for preparing |
| US6294214B1 (en) | 1994-02-24 | 2001-09-25 | The Procter & Gamble Co. | Noncarbonated beverage products with improved microbial stability and processes for preparing |
| US5445836A (en) * | 1994-05-12 | 1995-08-29 | Kraft Foods, Inc. | Enzymatic clarification of tea extracts |
| US5681569A (en) * | 1994-06-03 | 1997-10-28 | The Procter & Gamble Company | Beverage compositions containing green tea solids, electrolytes and carbohydrates to provide improved cellular hydration and drinkability |
| US5780086A (en) * | 1994-08-08 | 1998-07-14 | The Procter & Gamble Company | Color and shelf stable beverage compositions containing tea extract |
| US5427806A (en) * | 1994-08-08 | 1995-06-27 | The Procter & Gamble Company | Process for making a stable green tea extract and product |
| US6126980A (en) * | 1995-02-28 | 2000-10-03 | The Procter & Gamble Company | Noncarbonated beverage products having superior microbial stability and process for preparing same |
| CN1097438C (en) * | 1995-02-28 | 2003-01-01 | 普罗格特-甘布尔公司 | Preparation of noncarbonated beverage products having superior microbial stability |
| US6265008B1 (en) | 1995-02-28 | 2001-07-24 | The Procter & Gamble Co. | Preparation of noncarbonated beverage products having superior microbial stability |
| WO1996026648A1 (en) * | 1995-02-28 | 1996-09-06 | The Procter & Gamble Company | Preparation of noncarbonated beverage products having superior microbial stability |
| US5532012A (en) * | 1995-06-02 | 1996-07-02 | Thomas J. Lipton Co., Division Of Conopco, Inc. | Process for preparation of purified tea components using preconcentration by cream separation and solubilization followed by medium pressure chromatography and/or preparative HPLC |
| US5919512A (en) * | 1995-12-15 | 1999-07-06 | The Procter & Gamble Company | Method of making beverages having stable flavor/cloud emulsions in the presence of polyphosphate-containing preservative systems and low levels of xanthan gum |
| US5641532A (en) * | 1995-12-15 | 1997-06-24 | The Procter & Gamble Company | Beverages having stable flavor/cloud emulsions in the presence of polyphosphate-containing preservative systems by including gellan gum |
| US5792502A (en) * | 1995-12-15 | 1998-08-11 | The Procter & Gamble Company | Beverages having stable flavor/cloud emulsions in the presence of polyphosphate-containing preservative systems and low levels of xanthan gum |
| US6268009B1 (en) | 1996-02-26 | 2001-07-31 | The Procter & Gamble Company | Green tea extract subjected to cation exchange treatment and nanofiltration to improve clarity and color |
| US5879733A (en) * | 1996-02-26 | 1999-03-09 | The Procter & Gamble Company | Green tea extract subjected to cation exchange treatment and nanofiltration to improve clarity and color |
| US6063428A (en) * | 1996-02-26 | 2000-05-16 | The Procter & Gamble Company | Green tea extract subjected to cation exchange treatment and nanofiltration to improve clarity and color |
| US6274187B1 (en) * | 1996-06-19 | 2001-08-14 | Thomas J. Lipton Co., Division Of Conopco, Inc. | Aqueous tea extract concentrate stable at ambient temperature |
| US6024991A (en) * | 1996-06-19 | 2000-02-15 | Thomas J. Lipton Co., | Tea concentrate prepared by enzymatic extraction and containing xanthan gum which is stable at ambient temperature |
| US6036982A (en) * | 1996-06-19 | 2000-03-14 | Thomas J. Lipton Co., Division Of Conopco, Inc. | Enzymatically extracted tea concentrate with xanthan gum which is stable at ambient temperature |
| US6036991A (en) * | 1996-11-29 | 2000-03-14 | Lipton, Division Of Conopco, Inc. | Black leaf tea |
| WO1998023164A1 (en) * | 1996-11-29 | 1998-06-04 | Unilever Plc | Black leaf tea |
| US5922380A (en) * | 1996-12-12 | 1999-07-13 | Ito En, Ltd. | Tea manufacturing process |
| EP0891973A1 (en) * | 1997-07-15 | 1999-01-20 | Unilever Plc | Improvements in or relating to producing theaflavin |
| US6036986A (en) * | 1997-10-28 | 2000-03-14 | Lipton, Division Of Conopco, Inc. | Cinnamic acid for use in tea containing beverages |
| US6022576A (en) * | 1997-10-28 | 2000-02-08 | Lipton, Division Of Conopco, Inc. | Flavoring materials for use in tea containing beverages |
| WO1999021432A1 (en) * | 1997-10-28 | 1999-05-06 | Unilever Plc | Flavouring materials for use in tea containing beverages |
| US6120823A (en) * | 1997-10-28 | 2000-09-19 | Lipton, Divsion Of Conopco, Inc. | Flavoring materials used in foodstuffs |
| US6413570B1 (en) | 1999-02-12 | 2002-07-02 | Lipton, Division Of Conopco, Inc. | Tea concentrate |
| US20030069396A1 (en) * | 1999-11-29 | 2003-04-10 | Masakazu Nishimura | Neutralizing agent for toxin of microorganism belonging to the genus clostridium |
| US20060292247A1 (en) * | 1999-11-29 | 2006-12-28 | Masakazu Nishimura | Neutralizing agent for toxin of Clostridium microorganisms |
| US20050064050A1 (en) * | 1999-11-29 | 2005-03-24 | Masakazu Nishimura | Neutralizing agent for toxin of Clostridium microorganisms |
| US6468576B1 (en) * | 2000-06-23 | 2002-10-22 | Nestec S.A. | Frozen slush liquid concentrate and method of making same |
| US7815956B2 (en) | 2001-04-27 | 2010-10-19 | Pepsico | Use of erythritol and D-tagatose in diet or reduced-calorie beverages and food products |
| US20020197371A1 (en) * | 2001-04-27 | 2002-12-26 | Pepsico, Inc. | Use of erythritol and D-tagatose in zero-or low-calorie beverages and food products |
| US7579032B2 (en) | 2001-04-27 | 2009-08-25 | Pepsico, Inc. | Use of erythritol and D-tagatose in zero-or low-calorie beverages |
| US20070082106A1 (en) * | 2001-04-27 | 2007-04-12 | Thomas Lee | Use of Erythritol and D-Tagatose In Diet or Reduced-Calorie Beverages and Food Products |
| US20020160090A1 (en) * | 2001-04-27 | 2002-10-31 | Pepsico, Inc. | Use of erythritol and D-tagatose in diet or reduced-calorie beverages and food products |
| US20060068072A9 (en) * | 2001-04-27 | 2006-03-30 | Pepsico, Inc. | Use of erythritol and D-tagatose in diet or reduced-calorie beverages |
| US8221815B2 (en) | 2001-05-01 | 2012-07-17 | Pepsico, Inc. | Use of erythritol and D-tagatose in zero- or low-calorie beverages |
| US20090280232A1 (en) * | 2001-05-01 | 2009-11-12 | Pepsico., Inc. | Use Of Erythritol And D-Tagatose In Zero- Or Low-Calorie Beverages |
| US20020197379A1 (en) * | 2001-06-08 | 2002-12-26 | Unilever Bestfoods North America, Division Of Conopco, Inc. | Cold water soluble tea concentrate |
| US20030134017A1 (en) * | 2001-12-19 | 2003-07-17 | The Procter & Gamble Company | Beverage compositions having low levels of preservative with enhanced microbial stability |
| US8455031B2 (en) | 2001-12-19 | 2013-06-04 | The Procter & Gamble Company | Beverage compositions having low levels of preservative with enhanced microbial stability |
| US8263150B2 (en) | 2001-12-19 | 2012-09-11 | The Procter & Gamble Company | Beverage compositions having low levels of preservative with enhanced microbial stability |
| US20060153961A1 (en) * | 2002-07-31 | 2006-07-13 | Solorio Hector A | Reduced-calorie freezable beverage |
| US7094437B2 (en) * | 2002-07-31 | 2006-08-22 | Rich Products Corporation | Reduced-calorie freezable beverage |
| WO2004014142A1 (en) * | 2002-07-31 | 2004-02-19 | Rich Products Corporation | Reduced-calorie freezable beverage |
| US20040137126A1 (en) * | 2002-07-31 | 2004-07-15 | Solorio Hector A. | Reduced-calorie freezable beverage |
| WO2004054379A1 (en) * | 2002-12-16 | 2004-07-01 | Council Of Scientific And Industrial Research | A process for preparation of spiced tea concentrate and products thereof |
| US20050025872A1 (en) * | 2003-03-20 | 2005-02-03 | Joseph John F. | Non-dairy whippable food product |
| US7563470B2 (en) | 2003-03-20 | 2009-07-21 | Rich Products Corporation | Non-dairy whippable food product |
| US7351440B2 (en) | 2003-05-14 | 2008-04-01 | Rich Products Corporation | Whippable food product with improved stability |
| US7776376B2 (en) | 2003-05-14 | 2010-08-17 | Rich Products Corporation | Whippable food product with improved stability |
| US20040265468A1 (en) * | 2003-05-14 | 2004-12-30 | Cheryl Perks | Whippable food product with improved stability |
| WO2005053438A1 (en) | 2003-12-03 | 2005-06-16 | Unilever Plc | Tea beverage with improved flavour |
| US20080206429A1 (en) * | 2004-11-30 | 2008-08-28 | Nestec S.A. | Beverage Dispenser With Additive Dispensing |
| US7972639B2 (en) * | 2004-11-30 | 2011-07-05 | Nestec S.A. | Beverage dispenser with additive dispensing |
| US7976883B2 (en) * | 2004-11-30 | 2011-07-12 | Nestec S.A. | Method for delivering hot and cold beverages on demand in a variety of flavorings and nutritional additives |
| US20080020115A1 (en) * | 2004-11-30 | 2008-01-24 | Nestec S.A. | Method For Delivering Hot And Cold Beverages On Demand In A Variety Of Flavorings And Nutritional Additives |
| US20110206808A1 (en) * | 2005-03-03 | 2011-08-25 | Green Rabbit, Llc | Non-dairy, non-soy whippable food product and method of making |
| US20080160135A1 (en) * | 2006-12-27 | 2008-07-03 | Conopco, Inc., D/B/A Unilever | Method for Making a Tea Extract and a Tea Extract |
| US20100112157A1 (en) * | 2006-12-30 | 2010-05-06 | The Coca-Cola Company | Inhibition of the formation of tea opacification or precipitation in tea drinks during storage |
| WO2008082576A1 (en) * | 2006-12-30 | 2008-07-10 | The Coca-Cola Company | Inhibition of the formation of tea opacification or precipitation in tea drinks during storage |
| US20090092724A1 (en) * | 2007-10-04 | 2009-04-09 | David Mattie | Frozen Slush Drink |
| US20110143008A1 (en) * | 2007-10-04 | 2011-06-16 | David Mattie | Frozen Slush Drink |
| US20100051501A1 (en) * | 2008-08-29 | 2010-03-04 | International Business Machines Corporation | Ic waper carrier sealed from ambient atmosphere during transportation from one process to the next |
| US20110039009A1 (en) * | 2009-08-11 | 2011-02-17 | Curt Jones | Method and system for flash freezing tea-flavored liquid and making tea-based beverages |
| US20110123700A1 (en) * | 2009-11-25 | 2011-05-26 | Peththawadu Pasan Thijee | Instant liquid tea concentrate |
| US8367141B2 (en) * | 2009-12-21 | 2013-02-05 | Kao Corporation | Instant black tea containing green tea extract |
| WO2013036287A3 (en) * | 2011-09-09 | 2013-10-10 | Kraft Foods Group Brands Llc | Shelf stable, brewed beverage concentrates and methods of making the same |
| CN103917100A (en) * | 2011-09-09 | 2014-07-09 | 卡夫食品集团品牌有限责任公司 | Shelf stable, brewed beverage concentrates and methods of making the same |
| US9277758B2 (en) | 2011-09-09 | 2016-03-08 | Kraft Foods Group Brands Llc | Liquid coffee beverage concentrate |
| US20130224365A1 (en) * | 2012-02-28 | 2013-08-29 | Orly AVIDANILOVITCH | Frozen beverage portions |
| WO2015022130A1 (en) * | 2013-08-15 | 2015-02-19 | Unilever N.V. | A process for producing a liquid concentrate tea product |
| WO2015022123A1 (en) * | 2013-08-15 | 2015-02-19 | Unilever N.V. | A process for producing a liquid concentrate tea product |
| US10863754B2 (en) | 2014-07-03 | 2020-12-15 | Kraft Foods Group Brands Llc | Low water coffee and tea beverage concentrates and methods for making the same |
| US20220000139A1 (en) * | 2018-11-27 | 2022-01-06 | Conopco, Inc., D/B/A Unilever | A process of aroma recovery from tea leaf |
| US11737473B2 (en) * | 2018-11-27 | 2023-08-29 | Ekaterra Tea Manufacturing Usa Llc | Process of aroma recovery from tea leaf |
| US20220022514A1 (en) * | 2018-12-13 | 2022-01-27 | Societe Des Produits Nestle S.A. | Liquid concentrates formulated for dilution into nutritional products to promote safe swallowing for individuals with dysphagia |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4748033A (en) | Tea concentrate having freeze thaw stability and enhanced cold water solubility | |
| US4717579A (en) | Flowable frozen tea mix concentrate which contains high levels of sugar | |
| USH1628H (en) | Tea extract and process | |
| US7811619B2 (en) | Green tea beverage and method of making same | |
| US4946701A (en) | Beverages | |
| EP0675684B1 (en) | Process for manufacturing cold water soluble and chill stable ready to drink tea, and product | |
| CN102333458B (en) | Flavour enhancer and flavor compositions | |
| JP4958983B2 (en) | Containerized tea beverage | |
| KR101475758B1 (en) | Method for production of tea extract | |
| US20120294995A1 (en) | Fruit-juice-containing black tea beverage packed in a container and method for producing same | |
| EP2826381A1 (en) | Beverage containing tea leaf pectins | |
| JP3590028B2 (en) | Semi-fermented tea or fermented tea beverage with high catechin content | |
| JP3593108B2 (en) | How to make green tea flavor | |
| CA1230773A (en) | Soluble or disolved tea product | |
| US7022367B2 (en) | Oolong tea beverage and process of producing the same | |
| EP1576887B1 (en) | Packaged tea drink | |
| CA1316753C (en) | Tea concentrate having freeze/thaw stability and enhanced cold water solubility | |
| JP3511164B2 (en) | Tea extract for storage in closed container and method for producing the same | |
| JP3863482B2 (en) | Instant powder beverage | |
| JP2003304811A (en) | Production method of green tea polyphenol | |
| JP2021065130A (en) | Packed beverage and production method thereof | |
| JP4018435B2 (en) | STRICTININ RECOVERY METHOD, STRICTININ-CONTAINING METHOD, STRICTININ QUANTIFICATION | |
| JP2018166445A (en) | Condensed phosphate-containing beverage | |
| JP2021182884A (en) | Container-packed fruit juice-containing black tea beverage and production method thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FEPP | Fee payment procedure |
Free format text: PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY |
|
| STCF | Information on status: patent grant |
Free format text: PATENTED CASE |
|
| FPAY | Fee payment |
Year of fee payment: 4 |
|
| AS | Assignment |
Owner name: PROCETER & GAMBLE COMPANY, THE Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:LUO, XIACCHUN (NMN);PIAZZA, GARY ANTHONY;REEL/FRAME:006587/0486 Effective date: 19930520 |
|
| FPAY | Fee payment |
Year of fee payment: 8 |
|
| FPAY | Fee payment |
Year of fee payment: 12 |